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14121 total products found.
Picture for Understanding the Corrosion Performance and Mechanism of Stainless and Carbon Steels in Different Storage and Transportation of Pyrolysis Oil Environments
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Understanding the Corrosion Performance and Mechanism of Stainless and Carbon Steels in Different Storage and Transportation of Pyrolysis Oil Environments

Product Number: 51324-21226-SG
Author: Minkang Liu; Xue Han; Yimin Zeng
Publication Date: 2024
$40.00
This study assessed the suitability of two candidate materials for use in fast pyrolysis reactors and their core components. An immersion test conducted at temperatures of 60 °C and 80 °C over a 7- day period revealed significant corrosion in carbon steel A516-70, with corrosion rates reaching up to 6.24 mm/year. In contrast, UNS S32205 displayed impressive resistance to corrosion, even at 80 °C. Fe2O3 have been identified as the major corrosion products on A516-70, chromium oxides and spinel oxides were found on UNS S32205. The primary corrosive agents were identified as organic acids present in the pyrolysis oil, owing to the oil's high total acidic number and low pH value. Ongoing microscopic characterizations aim to provide a more comprehensive understanding of the underlying corrosion mechanisms.
Picture for Some Recent Corrosion Problems in Thermal Desalination Plants
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Some Recent Corrosion Problems in Thermal Desalination Plants

Product Number: 51319-12816-SG
Author: Roger Francis
Publication Date: 2019
$20.00

Copper alloys are widely used for the heat exchanger tubes in both multi-stage flash (MSF) and multiple effect distillation (MED) thermal desalination plants. Millions of metres of such tubing have been used and generally the copper alloys give good performance. In the last few years the author has looked at a number of failures from thermal desalination plants in the Middle East. These are not from one location but have occurred in different areas in different plants. The failure mechanisms are also different in each area. The common feature of the failures is that the corrosion mechanism for each one is well understood and they could all have been prevented by using a corrosion engineer at the design stage. This paper presents some of the diverse range of case studies and explains how they could have been prevented.
Picture for Investigation on Localized Corrosion Resistance of Nickel-based alloy UNS N07718 under Sour conditions of PuGuang Field simulated Environment
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Investigation on Localized Corrosion Resistance of Nickel-based alloy UNS N07718 under Sour conditions of PuGuang Field simulated Environment

Product Number: 51322-17761-SG
Author: Erfan Abedi Esfahani, Frederick Pessu, Jiong Qian, Anne Neville, Richard Barker
Publication Date: 2022
$20.00

Extremely corrosive environments of today’s oil and gas exploration requires more expensive Corrosion Resistant Alloys (CRAs) to be used for equipment such as tubulars. Material selection for oil and gas wells, especially those containing high hydrogen sulfide (H2S) and carbon dioxide (CO2) partial pressure, is very crucial. Hydrogen sulfide and carbon dioxide are quite aggressive to the materials used in oil field environments. The material of choice for these oil wells has to be reliable and cost-effective. This makes the material selection process a very complex and difficult task involving both financial and safety risks analysis.
Picture for Effect of Operating Parameters on the Corrosion of Candidate Heat Exchanger Alloys in Advanced Thermal Power Plants
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Effect of Operating Parameters on the Corrosion of Candidate Heat Exchanger Alloys in Advanced Thermal Power Plants

Product Number: 51324-21229-SG
Author: Minkang Liu; Yimin Zeng
Publication Date: 2024
$40.00
This study investigates the corrosion behavior of candidate steels with different Cr content in high-temperature s-CO2 environments and the influence of operating pressure. The results underscore the significant role of chromium, with content above 16 wt.% in the base metal proving effective in terms of conferring corrosion resistance. Moreover, the study reveals the substantial impact of operating pressure on weight gain, resulting in much thicker oxide layers. Further microscopic examinations may be required to gain deeper insights into oxide layer structure and composition. These findings advance our understanding of corrosion modes and extent within s-CO2 Brayton cycles.
Picture for 03330 ISOLATION OF POTENTIAL CORROSION INHIBITING
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03330 ISOLATION OF POTENTIAL CORROSION INHIBITING COMPOUNDS IN CRUDE OILS

Product Number: 51300-03330-SG
ISBN: 03330 2003 CP
Author: Sandra E. Hernandez, Jenny Bruzual, Francisco Lopez-Linares, Jose Gerardo Luzon
$20.00
Picture for Carbonate Stress Corrosion Cracking of Carbon Steel in Refinery FCC Main Fractionator Overhead Systems
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Carbonate Stress Corrosion Cracking of Carbon Steel in Refinery FCC Main Fractionator Overhead Systems

Product Number: 51390-90206-SG
Author: J.H. Kmetz, D.J. Truax
Publication Date: 1990
$20.00

Intergranular cracking and faiulure of carbon steel piping and vessels of FCC Main Fraqctionator overhead systems in NH3-H2S-CO2- containing environments is attributed to carbonate stress corrosion cracking. From plant water sampling program, cracking is correlated with water chemistry, open circuit potential and pH.
Picture for Corrosion Testing of Coatings in Simulated ORC Geothermal Heat Exchanger Environment
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Corrosion Testing of Coatings in Simulated ORC Geothermal Heat Exchanger Environment

Product Number: 51323-19444-SG
Author: Sigrun Nanna Karlsdottir, Adolph Jr. Manadao Bravo, Gifty Oppong Boakye, Halldór Pálsson, Andri Stefánsson
Publication Date: 2023
$20.00

Organic Rankin Cycle (ORC) geothermal power plants are commonly used in low-to-medium temperature fields with temperatures below 200 °C . The utilization of geothermal fluids to generate geothermal power or heating for district systems can be difficult due to dissolved species and gasses in the fluid. The problems often encountered are due to scaling and corrosion which are dependent on the pH, salinity, and composition of the geothermal fluid (e.g., CO2 and H2S) .
Picture for Control of Corrosion of Electrical Submersible Wells and Rod Pumped Wells in Varied Carbon Dioxide E
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Control of Corrosion of Electrical Submersible Wells and Rod Pumped Wells in Varied Carbon Dioxide Environments Using Batch Treatment

Product Number: 51317--9450-SG
ISBN: 9450 2017 CP
Author: Sunder Ramachandran
Publication Date: 2017
$20.00

This paper describes the performance of film persistent corrosion inhibitors that are effective at fairly high temperatures and in systems that see large amounts of carbon dioxide (CO2). Use of batch treatment with the correct chemical, at the proper frequency resulted in substantial decrease in operating cost.
Picture for The Influence Of Oxygen On Protective Iron Carbonate Scales Formed On Carbon Steel In CO2 Environments At Near-Neutral Ph
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The Influence Of Oxygen On Protective Iron Carbonate Scales Formed On Carbon Steel In CO2 Environments At Near-Neutral Ph

Product Number: 51322-17899-SG
Author: Pedro Netto da Silva, Gaute Svenningsen, Arne Dugstad, José Antônio da Cunha Ponciano Gomes
Publication Date: 2022
$20.00

High strength carbon steel tensile wires confined in the annulus of flexible pipes might experience corrosion when the annulus is flooded with water, either due to outer sheath breaches or to condensation of water molecules permeating from the bore through the inner sheath. Carbon dioxide (CO2) molecules may also permeate from the bore and reach the annulus, where it dissolves into water to form carbonic acid (H2CO3).
Picture for Influence of Alloying Elements on the Pitting Corrosion Resistance of CrMn Stainless Steels in Simulated Drilling Environments
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51315-5527-Influence of Alloying Elements on the Pitting Corrosion Resistance of CrMn Stainless Steels in Simulated Drilling Environments

Product Number: 51315-5527-SG
ISBN: 5527 2015 CP
Author: Helmuth Sarmiento Klapper
Publication Date: 2015
$20.00

 This paper presents the role of non-magnetic stainless steels' chemical composition on pitting corrosion susceptibility in chloride-containing solutions at different temperatures. Pitting and repassivation potentials of several grades were measured.
Picture for 02444 MANGANESE-DEPENDENT CORROSION...
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02444 MANGANESE-DEPENDENT CORROSION IN THE ELECTRIC UTILITY INDUSTRY

Product Number: 51300-02444-SG
ISBN: 02444 2002 CP
Author: W. H. Dickinson and R. W. Pick
$20.00
Picture for A New Method for Prioritizing Equipment in HTHA Service for Inspection and Replacement
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51316-7233-A New Method for Prioritizing Equipment in HTHA Service for Inspection and Replacement

Product Number: 51316-7233-SG
ISBN: 7233 2016 CP
Author: Jeremy Staats
Publication Date: 2016
$20.00

Background on High Temperature Hydrogen Attack (HTHA). Some current developments in HTHA inspection and mitigation. How several refiners have instituted an HTHA risk management plan for their refineries and the challenges and pitfalls they have encountered
Picture for Prediction of General and Localized Corrosion of Corrosion-Resistant Alloys in Aggressive Environments
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Prediction of General and Localized Corrosion of Corrosion-Resistant Alloys in Aggressive Environments

Product Number: 51319-12763-SG
Author: Ali Eslamimanesh
Publication Date: 2019
$20.00

A previously developed theoretical framework has been extended to predict the general and localized corrosion of various corrosion resistant alloys (CRAs) including alloys 2507 S13Cr 2535 28 and 29 in complex aqueous systems relevant to oil and gas production and aggressive process environments. For this purpose the model calculates the corrosion rates corrosion potential and repassivation potential as a function of temperature alkalinity pH partial pressure of gases (including H2S) and concentration of various aggressive and inhibitive species and organic or inorganic acids. The corrosion rates and potential are computed using the mixed-potential theory by considering the main anodic and cathodic reactions coupled with a rigorous thermodynamic model to account for speciation by solving phase and chemical equilibria. The repassivation potential is calculated from a model that simulates the phenomena at the interface of the alloy and the occluded solution environment. To enhance the predictive capabilities of the model the parameters of the repassivation potential model have been generalized as a function of alloy composition environment composition and temperature. The results show that the developed model reasonably represents and predicts the experimental corrosion potential repassivation potential and corrosion rate data from the literature.
Picture for 03554 DISSIMILATORY METAL REDUCING BACTERIA
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03554 DISSIMILATORY METAL REDUCING BACTERIA IN BIOGEOCHEMISTRY AND CORROSION

Product Number: 51300-03554-SG
ISBN: 03554 2003 CP
Author: Richard A. Royer, Richard F. Unz, Brian A. Dempsey, and William D. Burgos
$20.00
Picture for Volatile Corrosion Inhibitor (VCI) Testing – Pitfalls and Surprises in Routine Test Methods
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Volatile Corrosion Inhibitor (VCI) Testing – Pitfalls and Surprises in Routine Test Methods

Product Number: 51321-16323-SG
Author: Jonathan Brekan, Ph.D./Kristi Lanzo/Tammy Kovacs-Taborda
Publication Date: 2021
$20.00
Implication of Fractographic Analysis of the Crack in an Above Ground Pipeline – Potential Role of Hydrogen
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Implication Of Fractographic Analysis Of The In-Service Leak In An Above Ground Pipeline — Potential Role Of Hydrogen

Product Number: 51322-18022-SG
Author: Noelle Easter C. Co, Ming Gao, Ravi M. Krishnamurthy, Satya Kompally, Thomas Coates
Publication Date: 2022
$20.00

Fracture surface morphology is useful in determining the mechanisms involved in cracking. Features in the fracture surface of steel like micro-void coalescence or dimples are often related to ductile crack mode, while features like cleavage, and rock-candy showing grain boundary cracking are commonly related to brittle crack mode. Some fracture surface may have a predominant feature, while others may have presence of mixed features. Types of stress corrosion cracking (SCC) are commonly identified by the features present in the fracture surface. Features showing transgranular quasi-cleavage cracking are often related to near-neutral pH SCC, while features that show rock-candy intergranular cracking are often related to high-pH SCC [1].
Picture for 01325 NICKEL BASE ALLOYS: CORROSION CHALLENGES
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01325 NICKEL BASE ALLOYS: CORROSION CHALLENGES IN THE NEW MILLENNIUM

Product Number: 51300-01325-SG
ISBN: 01325 2001 CP
Author: D.C.Agarwal and Jutta Kloewer
$20.00
Picture for Evaluation of Hydrogen Embrittlement Resistance of 41XX Cr-Mo steels, 13Cr Stainless Steel in High Pressure Hydrogen Environment
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Evaluation of Hydrogen Embrittlement Resistance of 41XX Cr-Mo steels, 13Cr Stainless Steel in High Pressure Hydrogen Environment

Product Number: 51323-18971-SG
Author: Karthik Krishnan, Shashwat Shukla, Arpana Verma
Publication Date: 2023
$20.00

Hydrogen gas (H2) is touted for potential as future fuel as it could be a way to convert excess energy produced when demand is lower. Depending on the source of excess energy used for conversion to Hydrogen this process could have low or no carbon footprint. This Hydrogen gas could then be stored and used for electricity, transportation, chemical processes when the demand arises similar to how natural gas is being used currently. Thus, storage of Hydrogen in vast volumes would be one of the key elements for the success of Hydrogen as a future fuel
Picture for Corrosion Films Formed in CO2 Saturated Conditions on In-Situ Corrosion of X65 Pipeline Steel
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51313-02188-Corrosion Films Formed in CO2 Saturated Conditions on In-Situ Corrosion of X65 Pipeline Steel

Product Number: 51313-02188-SG
ISBN: 02188 2013 CP
Author: Xinming Hu
Publication Date: 2013
$20.00
Picture for Predicting Hot Oil Corrosion: A Framework for Quantifying Reactive Organic Sulfur Compounds in Crude Unit Process Streams
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Predicting Hot Oil Corrosion: A Framework for Quantifying Reactive Organic Sulfur Compounds in Crude Unit Process Streams

Product Number: 51323-19105-SG
Author: Winston Robbins, Sridhar Srinivasan, Gerrit Buchheim
Publication Date: 2023
$20.00

In Corrosion/2021, the authors introduced a molecular mechanistic model that quantifies and predicts SNAPS corrosion rates. During Corrosion/2022, we presented the mechanistic corrosion prediction framework describing the molecular basis of the model’s reactions, kinetics, and mass transport of ROSC to vessel walls. In this molecular model, sulfidation corrosion is calculated for direct heterolytic reaction of ROSC with solid surfaces.
Picture for Modelling Electrolytic Hydrofluoric Acid In The Fractionation Phase Change Corrosion Zone Of HF Alkylation Units
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Modelling Electrolytic Hydrofluoric Acid In The Fractionation Phase Change Corrosion Zone Of HF Alkylation Units

Product Number: 51322-17520-SG
Author: Andy C. Gysbers, J. Tim Korstanje, Michael S. Cayard, Peiming Wang, Ezequiel Vincent
Publication Date: 2022
$20.00

Hydrofluoric acid (HF) is used as a catalyst in the alkylation process to react isobutane with olefin feeds to manufacture a high octane alkylate product used in gasoline blending. The HF catalyst is added in its anhydrous liquid form (< 400 ppmw H2O) but as it circulates in the reaction system, residual water in the Paper No. 17520 liquid hydrocarbon feed is absorbed by the acid such that the circulating reaction acid builds up a small percentage (0.5 to 2.0 mass%) of water. This water/HF mixture is also referred to as rich HF (RHF). In addition, the alkylation reactions also will generate fluorocarbons and acid soluble oils (ASOs).
Picture for 99243 COMPUTER MODELING OF CORROSION IN
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99243 COMPUTER MODELING OF CORROSION IN ABSORPTION COOLING CYCLES

Product Number: 51300-99243-SG
ISBN: 99243 1999 CP
Author: Andrzej Anderko and Robert D. Young
$20.00
Picture for Investigation of the Corrosion Performance of Stainless Steel and Low Alloy Steel Sucker Rod Materials in Aggressive Environments
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Investigation of the Corrosion Performance of Stainless Steel and Low Alloy Steel Sucker Rod Materials in Aggressive Environments

Product Number: 51320-14321-SG
Author: Aleksey Shakhmatov, Oscar Martinez, Robert Badrak, Sergey Kolesov, Rodrigo Barreto, William Howie
Publication Date: 2020
$20.00

The corrosion resistance of sucker rod materials can be a significant concern, especially in aggressive service environments with high acid gas concentrations. Corrosion-related failures have been associated with increased levels of produced hydrogen sulfide (H2S) and carbon dioxide (CO2). The presence of corrosion damage, which is characterized by local material dissolution and pitting formation under the influence of CO2 and/or H2S, provides the initiation sites in a fatigue cracking mechanism. The fatigue crack propagation in corrosion aggressive environments is associated with the following factors: (1) local tensile stress concentration at crack tip, and (2) local corrosion dissolution. Therefore, using a material that tends to re-passivate as it interacts with the environment would be the optimum solution in order to mitigate the likelihood of field failures and reduce overall operating costs. Regarding passive film disruption processes abrasion and high temperature influences were not considered at this stage of the present study and repassivation kinetics were not measured. Conventional sucker rod production processes include normalize and temper (N&T) or quench and temper (Q&T) heat treatments to meet desired strength levels of low alloy steels. In order to enhance the corrosion properties and provide a resistant sucker rod solution, 13Cr martensitic stainless steel may provide a viable alternative to low alloys steels. This paper focuses on the characterization of 13Cr sucker rod material by comparing the general corrosion and corrosion fatigue performance with low-alloy steels. 
Picture for Cathodic Prevention/Protection Of Marine Corrosion Of Steel In Previously Cracked Concrete
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Cathodic Prevention/Protection Of Marine Corrosion Of Steel In Previously Cracked Concrete

Product Number: 51321-16952-SG
Author: M. Dugarte; A.A. Sagüés
Publication Date: 2021
$20.00
Picture for 07254 Study of Corrosion in Erosion-Corrosion of Two Stainless Steels in Simulated Marine Conditions
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07254 Study of Corrosion in Erosion-Corrosion of Two Stainless Steels in Simulated Marine Conditions via Experimental Design

Product Number: 51300-07254-SG
ISBN: 07254 2007 CP
Author: Xinming Hu, Hang Meng, and Anne Neville
Publication Date: 2007
$20.00
Picture for Factors Influencing Droplet Corrosion in Dense Phase CO2
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Factors Influencing Droplet Corrosion in Dense Phase CO2

Product Number: 51319-13017-SG
Author: Ralph Baessler
Publication Date: 2019
$20.00

Recent studies have shown that even at a very low concentration of impurities (less than 100 ppmv of SO2 NO2 O2 and H2O) the droplet formation and condensation of sulfuric and nitric acids in dense phase CO2 are possible and observable. To reveal the mechanism of droplet corrosion in dense CO2 at high pressure and low temperature further studies on factors that affect wettability and resulting corrosion behaviors of transport pipeline steels are needed.In this work carbon steels (X52 X70) martensitic steel UNSS41500 and superaustenite UNS08031 were examined not only in static but also dynamic CO2 stream with either oxidizing (SO2 NO2 O2) or reducing (H2S and H2) impurities. Exposure tests with and without CO2 saturated water droplets were performed at both low temperature (278 K) and high temperature (313 K) at high pressure where CO2 is supercritical or in dense phase. To reveal the effects of surface morphology carbon steel coupons with different surface roughness were prepared not only to measure the wettability by contact angle but also to expose to CO2 stream containing oxidizing/reducing impurities to observe the condensation and possible droplet corrosion that followed. Two-week exposed coupons showed no condensation at 313 K 10 MPa and 50 ppmv H2O indicating the important role of temperature on the possibility of condensation regardless the type of impurities and flow rate. At 278 K the result from exposure tests signified the role of oxidizing impurities on the condensation and the droplet corrosion that followed. Although different surface roughness resulted in different wetting behaviors and therefore the measured contact angles it did not significantly influence the corrosion process upon long time exposure. This is attributed to the change of wetting behavior due to corrosion products that covered the carbon steel surface during exposure test.
Picture for 10317 Corrosion Performance of Alloy 29 in Simulated Sour Environments
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10317 Corrosion Performance of Alloy 29 in Simulated Sour Environments

Product Number: 51300-10317-SG
ISBN: 10317 2010 CP
Author: Katarina B. Persson, Shamus J. Kaukas and Ulf H. Kivisäkk
Publication Date: 2010
$20.00
Picture for Method of Conduction Controlled Velocity Laboratory Corrosion Tests
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TM0270-HD1972-SG-Method of Conduction Controlled Velocity Laboratory Corrosion Tests-HD1972

Product Number: 21202-HD1972
Author: NACE
Publication Date: 1972
$179.00

Conducting controlled velocity corrosion tests in the laboratory wherein a corrosive solution may be moved at a known tangential velocity across the face of corrosion test specimens. Historical Document 1972
Picture for 10076 Corrosion of Metals in Biodiesel from Pongamia Pinnata
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10076 Corrosion of Metals in Biodiesel from Pongamia Pinnata

Product Number: 51300-10076-SG
ISBN: 10076 2010 CP
Author: H.N Meenakshi, Anisha Anand, R. Shyamala and Sankara Papavinasam
Publication Date: 2010
$20.00
Picture for Electrochemical Characterization of Advanced Titanium Alloys in Simulated Physiological Environments
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51315-6120-Electrochemical Characterization of Advanced Titanium Alloys in Simulated Physiological Environments

Product Number: 51315-6120-SG
ISBN: 6120 2015 CP
Author: Vilupanur Ravi
Publication Date: 2015
$20.00
Picture for Combined Effects of Microbes and Nitrate on SRB Growth Souring and Corrosion
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Combined Effects of Microbes and Nitrate on SRB Growth Souring and Corrosion

Product Number: 51317--9425-SG
ISBN: 9425 2017 CP
Author: Bei Yin
Publication Date: 2017
$20.00

A stationary testing method and a porous media flow reactor method were used for these studies. The effect of different NRB, including NO2NRB and sulfide-oxidizing NRB (SONRB) on corrosion of carbon steel beads in the presence and absence of nitrate was also investigated using porous media flow reactors.
Picture for 03431 CORROSION MONITORING IN OIL AND GAS
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03431 CORROSION MONITORING IN OIL AND GAS PRODUCTION

Product Number: 51300-03431-SG
ISBN: 03431 2003 CP
Author: M.J.J. Simon Thomas and S. Terpstra
$20.00
Picture for Corrosion of Pipelines in a Crude Oil Storage Facility
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AC Corrosion of Pipelines

Product Number: 37656-pdf
ISBN: 978-1-57590-464-1
Author: Y. Frank Cheng
$160.00

AC Corrosion of Pipelines covers the essential topics related to AC corrosion of pipelines, a problem affecting the safety and reliability of underground pipelines. In addition to the basic principles of AC interference induced by adjacent AC power lines and other sources, the book details the adverse effects of the interference on collocated pipelines, including corrosion and pitting corrosion, coating degradation, deviating of cathodic protection potentials, and the ineffectiveness of cathodic protection systems. Moreover, effective management measures to this problem are discussed. It also covers the DC interference and DC corrosion of the pipelines, as compared to the AC corrosion phenomenon. The book, the first of its kind, provides a complete and comprehensive understanding to the phenomenon from both the fundamentals and the author's research experiences.

The reader can learn and understand the basics associated with AC corrosion. Moreover, the book provides solutions and industry practice to mitigate, control, and manage AC corrosion of pipelines. The reader can thus learn the appropriate solutions to the problem. Finally, the book also includes DC corrosion of pipelines, in addition to AC corrosion, another essential problem to the buried pipelines with the increasing development of HVDC power lines. All of them contribute to improved knowledge base and recommended solutions for the actual problem threating the integrity and safety of pipelines.
Failure Analyses On A Super Duplex Stainless Steel Tube Material Before And After Slow Strain Rate Testing In Sour Conditions – Part 1: SCC Susceptibility
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Failure Analysis On A Super Duplex Stainless Steel Tube Material Before And After Slow Strain Rate Testing In Sour Conditions - Part 1: SCC Susceptibility

Product Number: 51322-17998-SG
Author: Wenle He, Raveendra Siriki, Jerry Lindkvist
Publication Date: 2022
$20.00

Standards NACE(1) MR0175 / ISO(2) 15156-31 have temperature-H2S-Cl-pH limits for safely using duplex stainless steels based on their Pitting Resistance Equivalent Number (PREN) of subcategory such as duplex stainless steel (DSS, PREN 30-40, Mo>1.5%) and super duplex stainless steel (SDSS, PREN 4045), temperature-pH domain of stress corrosion cracking (SCC) resistance can be used for material evaluation and provided by using slow strain rate testing (SSRT) screening in sour testing conditions2. 
Picture for 00237 FIRESIDE CORROSION IN KRAFT RECOVERY
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00237 FIRESIDE CORROSION IN KRAFT RECOVERY BOILERS LOWER FURNACE

Product Number: 51300-00237-SG
ISBN: 00237 2000 CP
Author: Preet M. Singh, Safaa J. Al-Hassan, Slaone Stalder, and Greg Fonder
$20.00
Picture for 01184 CHARACTERIZATION OF DEPOSITS AND THEIR
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01184 CHARACTERIZATION OF DEPOSITS AND THEIR INFLUENCE ON CORROSION IN WASTE INCINERATION PLANTS IN DENMARK

Product Number: 51300-01184-SG
ISBN: 01184 2001 CP
Author: M. Montgomery, O.H. Larsen
$20.00
Picture for A Novel Corrosion Rate Monitoring Method For Steel In Soil Based On Tafel Extrapolation Method
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A Novel Corrosion Rate Monitoring Method For Steel In Soil Based On Tafel Extrapolation Method

Product Number: 51321-16967-SG
Author: Satoru Yamamoto; Masaru Abe; Kenkichi Tashiro
Publication Date: 2021
$20.00
Picture for Flow Accelerated Corrosion of Carbon Steel Pipe Carrying Hot Condensate Water in a Chemical Plant
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51316-7127-Flow Accelerated Corrosion of Carbon Steel Pipe Carrying Hot Condensate Water in a Chemical Plant

Product Number: 51316-7127-SG
ISBN: 7127 2016 CP
Author: Fengmei Song
Publication Date: 2016
$20.00

Multiple leaks occurred with a carbon steel pipe carrying hot condensate water (300F and 140 psi).  A root cause analysis was performed, including visual and metallographic examination of two failed samples chemical, analysis of weld metal and base metal and chemical analysis of water samples.  Results show that flow accelerated corrosion (FAC) was the responsible mechanism leading to the failures.
Picture for SP0196-2020, Galvanic Anode Cathodic Protection of Internal Submerged Surfaces of Steel Water Storage Tanks
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SP21461-2020, Corrosion Evaluations of Masonry Clad Steel Frame Buildings (Pre-1950)

Product Number: SP21461-2020
ISBN: 1-57590-409-8
Publication Date: 2020
$109.00

When distress of a structure is evident, it is important to determine the nature of the degradation to select the best restoration strategy.  This standard practice provides testing procedures and investigative techniques for the evaluation of masonry-clad steel frame buildings.  The investigation and evaluation techniques described in this standard focus on degradation resulting from corrosion of the steel frame. 

This standard provides the investigator, corrosion specialist, engineer, or owner a framework for evaluating the corrosion condition of a steel frame building beyond simple visual inspection and basic sounding techniques.  Evaluation techniques that identify general and localized corrosion of masonry-clad steel frame buildings are provided.

This standard is intended for use by corrosion specialists, historic architects, structural engineers, and exterior building envelope consultants involved with evaluating corrosion of steel frame buildings and the subsequent effect on the masonry cladding.  It also may be useful to owners of historic buildings whose service life may be affected by steel frame corrosion.
Preventive Maintenance in Older Facilities
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Preventive Maintenance in Older Facilities

Product Number: 41208-462-SG
Author: Bruce Woodruff
Publication Date: 2008
$20.00

 Many industries are operating under severely limited O&M budgets and have been for some time. “Lean and mean” in today’s reality has become “mal-nourished and over stressed”. The last major corrosion study conducted in our industry showed a $276 Billion/Yr. deficit of which 75% was unrecoverable. Now a new study has determined that it is never too late to restore measurable viability to a facility's operation through adequate and proper preventive maintenance. This is good news, providing we can adequately demonstrate and use it.
Picture for Corrosion Assessment of Stainless Steels in Nitric Acid
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51315-5600-Corrosion Assessment of Stainless Steels in Nitric Acid

Product Number: 51315-5600-SG
ISBN: 5600 2015 CP
Author: Daniel Gullberg
Publication Date: 2015
$0.00
Picture for Modeling Abrasion-Corrosion in Horizontal Pipeline Slurry Flows
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Modeling Abrasion-Corrosion in Horizontal Pipeline Slurry Flows

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

Slurry pipeline systems are used to process and transport mined ore and tailings in the oil and gas and mining industries. The handling processing and transporting of these slurries result in significant pipe wall material losses or wear. For the most widely used material carbon steel these losses are attributed to the combined effects of erosion/abrasion and corrosion due to the exposure of pipe wall materials to an aerated mixture of solids and liquids. In an attempt to mitigate this challenge some end-users such as mined oil sands operators have adopted polymer based pipe liner which basically only experiences erosion or abrasion damage. Models can be used as a predictive tool to optimize slurry design and processes material selection and/or even used as a tool for preventive maintenance. They are also being employed for technology assessment and product evaluation. These benefits are realized if the models are based on underlying mechanics or phenomena in the real systems. Unarguably there are a significant number of models for erosion-corrosion especially erosive wear. These models have a varying degree of accuracy which is partly due to the fact that most of them are based on some degree of empiricism and may lack accurate information on key parameters. Unfortunately models for wear which usually occurs in dense slurries are very limited despite most slurry applications fall under this category. As part of a broader wear model development project at our company this work focuses on validations of existing abrasive wear and/or abrasive-corrosion models. This work adopts computational fluid dynamic (CFD) as a tool to model abrasive wear and/or abrasion-corrosion in horizontal pipeline dense slurries. These CFD results will be compared with previously acquired wear data in our pilot-scale slurry flow loop for mild and dual-phase stainless steels pipe spools. The model performance will be presented and discussed with recommendations for future works.Key words: Wear; Pipeline; Slurry; Oil sands; Abrasion-corrosion; Flow Loop; CFD; modeling
Corrosion and Materials Fundamentals for Engineers in Wastewater Treatment Plants & Collection Systems, 3rd Edition

Corrosion and Materials Fundamentals for Engineers in Wastewater Treatment Plants & Collection Systems, 3rd Edition

Product Number: 37609-POD
ISBN: 978-1-57590-327-9
$105.00

For engineers and maintenance personnel who design, operate, and maintain large, multi–stage wastewater treatment plants (WWTP) Basics of corrosion of metals and degradation of non–metals, including concrete, and how to mitigate them.  3rd edition 2016 NACE
Picture for Update on Corrosion Performance of CBPC Coatings in Aggressive Bridge Environment
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51317--9593-Update on Corrosion Performance of CBPC Coatings in Aggressive Bridge Environment

Product Number: 51317--9593-SG
ISBN: 9593 2017 CP
Author: Md Ahsan Sabbir
Publication Date: 2017
$20.00

Chemically Bonded Phosphate Ceramic coating was investigated in various environments such as inland, beach and salt-fog exposure. After 8-month outdoor testing, the coating was evaluated by visual inspection, coating thickness, adhesion measurement and X-ray diffraction. Long term testing ensued, up to 24 months.

 
Picture for 97107 CORROSION SURVEILLANCE IN SPENT FUEL
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97107 CORROSION SURVEILLANCE IN SPENT FUEL STORAGE POOLS

Product Number: 51300-97107-SG
ISBN: 97107 1997 CP
Author: James P. Howell
$20.00
Picture for 08081 Corrosion of Copper Braze Alloys in Sulfide Containing Water
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08081 Corrosion of Copper Braze Alloys in Sulfide Containing Water

Product Number: 51300-08081-SG
ISBN: 08081 2008 CP
Author: Yar-Ming Wang, David Sigler, and Dusanka Radovic
Publication Date: 2008
$20.00
Picture for Impact of oxygen pollution on H2S corrosion and hydrogen permeation
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51318-10931-Impact of oxygen pollution on H2S corrosion and hydrogen permeation

Product Number: 51318-10931-SG
Author: Martien Duvall Deffo Ayagou / Christophe Mendibide / Claude Duret-Thual / Jean. Kittel / Nicolas Ferrando
Publication Date: 2018
$20.00

It is well known that H2S promotes hydrogen entry into steels that may result in many types of steel failures. This paper examines the influence of traces of oxygen on corrosion and hydrogen charging of steel in an H2S containing environment.
Picture for 99619 ENVIRONMENTAL EFFECTS IN FLOW-ASSISTED
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99619 ENVIRONMENTAL EFFECTS IN FLOW-ASSISTED CORROSION OF NAVAL SYSTEMS

Product Number: 51300-99619-SG
ISBN: 99619 1999 CP
Author: David A. Shifler, PhD, PE
$20.00

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