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Picture for Corrosion Behavior of UNS N08935 In Refinery Sour Water Services
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Corrosion Behavior of UNS N08935 In Refinery Sour Water Services

Product Number: 51321-16831-SG
Author: Karen Picker; Josefin Eidhagen; Jonas Howing
Publication Date: 2021
$20.00
Picture for Corrosion Behavior Of UNS S31600 In Purified Molten Salts
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Corrosion Behavior Of UNS S31600 In Purified Molten Salts

Product Number: 51321-16945-SG
Author: Chi Ying Loh; Jared O. Butner; Connor J. Veronese; Christopher J. Faraj; Chi Ying Loh; Jared O. Butner; Connor J. Veronese; Christopher J. Faraj; Vilupanur A. Raviilupanur A. Ravi
Publication Date: 2021
$20.00
Picture for Corrosion Behavior of Zinc Cold Spray Coatings (ZnCr & ZnNb) in a Simulated Natural Gas Environment Containing H2O, CO2, and H2S
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Corrosion Behavior of Zinc Cold Spray Coatings (ZnCr & ZnNb) in a Simulated Natural Gas Environment Containing H2O, CO2, and H2S

Product Number: 51324-20451-SG
Author: Zineb Belarbi; Richard E. Chinn; Ömer N. Doğan
Publication Date: 2024
$40.00
Internal corrosion and sulfide stress cracking (SSC) are problems for steel pipelines transporting natural gas or CO2 containing partial pressures of H2S higher than 0.3 kPa (0.05 psi). The objective of this work is to mitigate internal corrosion and SSC in steel pipelines transporting natural gas containing H2S using cold spray coatings. Two types of the cold spray binary metallic coatings (zinc chromium (ZnCr), zinc niobium (ZnNb)) were studied using electrochemical techniques: potentiodynamic polarization (PDP), linear polarization resistance (LPR), and electrochemical impedance spectroscopy (EIS). The evaluation of the corrosion resistance of cold spray coatings (ZnCr, ZnNb) was carried out in an environment containing 4 bar CO2 pressure, simulating the partial pressures that are found in gas transmission lines over a solution of 3.5 wt.% NaCl heated to 40 °C. To simulate sour conditions, a concentration of 0.003 M Na2S2O3.5H2O, which corresponds to H2S partial pressures around 0.079 bar (1.146 psi), was used. Post-corrosion surface characterization was performed using a scanning electron microscope (SEM) equipped with energy-dispersive X-ray spectroscope (EDS) and X-ray diffraction analysis (XRD). The data showed that the presence of 0.003 M Na2S2O3.5H2O shifted the corrosion potential to more anodic values and decreased the corrosion current density. Bothcoatings showed similar behavior after 1 hour of exposure in CO2/H2S environment, which indicated that similar electrochemical reactions were taking place on ZnNb and ZnCr. SEM images and EDS surface analyses for specimens showed a significant change in surface chemical composition of carbon steel coated with ZnNb and ZnCr, after 24 hours of immersion. No localized attack was observed. The EDS analysis and XRD results revealed the presence of zinc sulfide (ZnS).
Picture for Corrosion Behaviour and Studies on Effect of Electric Arc Furnace Dust Addition on Porosity and Chloride Diffusion in Concrete
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Corrosion Behaviour and Studies on Effect of Electric Arc Furnace Dust Addition on Porosity and Chloride Diffusion in Concrete

Product Number: 51324-20421-SG
Author: Fahad M. Al Mutlaq; Saad A. Al-Shehri; Saud Al Subai
Publication Date: 2024
$40.00
The rate of deterioration of concrete structures is normally affected by the rate at which harmful substances can penetrate into the concrete. Aggressive substances can move into concrete by different transport mechanisms. The main transport mechanisms that could promote the deterioration of concrete structures are diffusion, permeation, capillary absorption and migration. The rate of chloride penetration into concrete has been found to depend on many factors including the porosity and permeability of concrete. Accordingly, concrete porosity is one of the most important parameters that influences the durability of concrete. Furthermore, when the concrete structures are subjected to aggressive environments such as marine environments the primary transport mechanism of chloride ion ingress is often diffusion. For that reason, the chloride diffusivity and porosity are very important durability parameters since they may play a major role in accelerating deterioration and thus reducing the service life of structure. Intensive experimental works were carried out where cement pastes specimens and concrete mixes were prepared at different w/c ratios mixed with 0, 2 and 3 % Electric Arc Furnace Dust addition. The results are very promising and revealed that addition of Electric Arc Furnace Dust (EAFD) reduced the coarse capillary porosity effectively and improved resistance to chloride ingress into concrete, hence this will improve corrosion resistance of reinforced concrete structures located in aggressive marine environment. More details in the results can be found in this paper.
Picture for Corrosion Behaviour of Solution Precursor Plasma-Sprayed TiO2/Al2O3 Composite Coatings for Heat Exchanges
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Corrosion Behaviour of Solution Precursor Plasma-Sprayed TiO2/Al2O3 Composite Coatings for Heat Exchanges

Product Number: 51321-16304-SG
Author: Garima Mittal; Francesco Fanicchia; Imran Bhamji; Shiladitya Paul
Publication Date: 2021
$20.00
	Picture for Corrosion by Elemental Sulphur Deposition in Natural Gas Transmission Systems
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Picture for Corrosion Challenges in Processing Crude Oils: Influence of Active Sulfur Species and Corrosion Rates of Various Alloys
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Corrosion Challenges in Processing Crude Oils: Influence of Active Sulfur Species and Corrosion Rates of Various Alloys

Product Number: 51324-21207-SG
Author: Yuhchae Yoon; Hui Li; Russell D. Kane
Publication Date: 2024
$40.00
The depletion of conventional sweet oil resources has led to increased attention towards sour and acidic oil sources, which typically consist of lower-quality, corrosive crude oils with elevated concentrations of naphthenic acids and sulfur compounds. They are often referred to as “opportunity crudes” since they come at a lower price to refiners, but if successfully processed, they can result in a higher margin to the refinery. This paper focuses on an investigation of the impact of active sulfur species present in crude oils during processing. Corrosion rates of several common alloys were evaluated under stirred/pipe flow conditions in autoclaves. The experimental conditions closely simulated relevant refinery environments, encompassing temperatures ranging from 200°C to 370°C. The study assessed the influence of temperature, wall shear stress (WSS), and active sulfur content on corrosion rates. The results were derived from a comprehensive Joint Industry Program (JIP) conducted to quantify the influence of crude oil chemistry on naphthenic acid corrosion, understand the contributions of active sulfur chemistry to protection and FeS scale formation. The program also assessed the ability to resist naphthenic acid corrosion by utilizing beneficial sulfur speciation in the context of operational factors such as temperature and wall shear stress to build a prediction model to characterize the active sulfur level as a function of sulfur compound concentration and temperature, which is further utilized to predict corrosion rates of multiple alloys.