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Picture for Electrochemical Injection of Corrosion Inhibitors and Chloride Extraction for Protection of Steel Reinforcement
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Electrochemical Injection of Corrosion Inhibitors and Chloride Extraction for Protection of Steel Reinforcement

Product Number: 51319-13451-SG
Author: Milan Kouril
Publication Date: 2019
$20.00
Picture for Electrochemical Investigation Into the Influence of Monoethylene Glycol on CO2 Corrosion in the Presence of Acetic Acid
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Electrochemical Investigation Into the Influence of Monoethylene Glycol on CO2 Corrosion in the Presence of Acetic Acid

Product Number: 51321-16332-SG
Author: Md Mayeedul Islam/Rolf Gubner/Thunyaluk Pojtanabuntoeng
Publication Date: 2021
$20.00
Picture for Electrochemical Investigation Of Alloys For Alkaline Water Electrolyzers
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Electrochemical Investigation Of Alloys For Alkaline Water Electrolyzers

Product Number: 51321-16975-SG
Author: Morten Tjelta; Simona Palencsar, Jon Kvarekvål
Publication Date: 2021
$20.00
Picture for Electrochemical Investigation of Duplex Stainless Steel Cladded Carbon Steel Manufactured via Powder
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Electrochemical Investigation of Duplex Stainless Steel Cladded Carbon Steel Manufactured via Powder

Product Number: 51319-13538-SG
Author: Pratik Murkute
Publication Date: 2019
$20.00

The duplex stainless steels find extensive applications where there is a need for highly corrosion resistant materials i.e. oil and gas industry nuclear power generation seawater applications. This study aims to investigate the electrochemical and corrosion properties of duplex stainless steel cladded carbon steel manufactured using powder bed the selective laser melting (PB-SLM) technique in 3.56 wt.% NaCl solution. The PB-SLM technique involves spreading of a thin layer of duplex stainless steel powder on a mild steel substrate and localized melting with Yb - fiber laser. Crucial parameters of the PB-SLM process such as laser power laser-scanning speed and layer thickness were optimized and fine-tuned to achieve the best possible bonding between the clad material and the carbon steel substrate. Using the optimized process parameters carbon steel substrates were cladded with stainless steel of various thicknesses. Several mechanical and microscopic tests (viz. nano-indentation X-ray diffraction Scanning electron microscopy) were performed to characterize both the bulk properties of the stainless steel layer and the interface between the cladding and the substrate. Electrochemical and corrosion properties were tested via. open-circuit potential monitoring electrochemical impedance spectroscopy (EIS) and cyclic polarization (CP) in the said electrolyte. Scanning vibrating electrode technique was employed to study the galvanic corrosion properties of the duplex stainless steel and carbon steel at the clad-substrate interface.

Picture for Electrochemical Investigation of the Integrity of Cathodic Protection MMO Anodes in the Presence of Vapor Corrosion Inhibitors
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Electrochemical Investigation of the Integrity of Cathodic Protection MMO Anodes in the Presence of Vapor Corrosion Inhibitors

Product Number: 51324-21177-SG
Author: Juan Dominguez Olivo; Terry Natale; Sujay Math
Publication Date: 2024
$40.00
Picture for Electrochemical Model of CO2 Corrosion in the Presence of Quaternary Ammonium-type Corrosion Inhibitor Model Compounds
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Electrochemical Model of CO2 Corrosion in the Presence of Quaternary Ammonium-type Corrosion Inhibitor Model Compounds

Product Number: 51319-13392-SG
Author: Juan Dominguez Olivo
Publication Date: 2019
$20.00

The oil and gas industry utilize surfactant-type organic corrosion inhibitors as a way to mitigate internal pipeline corrosion. Changes in corrosion rates due to inhibitor addition have been related to adsorption isotherms as a function of the inhibitor concentration. However the question as to how a corrosion inhibitor affects the electrochemical reactions governing CO2 corrosion remains unclear. This research proposed to investigate the aforementioned question by using a systematic approach: four different corrosion inhibitors synthesized in-house were utilized to determine the effect of the tail length on the activation energy of the electrochemical process underlying the corrosion of an API 5L X65 steel in CO2 corrosion at pH 4. The corrosion inhibitors all contained the same head group (dimethyl-benzyl-ammonium) with four different alkyl tail lengths (C4 C8 C12 and C16). A theoretical description of the increase in the activation energy of the electrochemical process underlying CO2 corrosion due to the presence of the corrosion inhibitors was proposed. Such a description also led to the development of a modified Butler-Volmer equation that describes the retardation in charge transfer rates of the electrochemical reactions associated with the corrosion of mild steel. The model is based upon changes in activation energy calculated by an Arrhenius plot. The model was compared with experimental potentiodynamic sweeps for each corrosion inhibitor model compound. As a result the corrosion model predicts the corrosion rate and the open circuit potential in the presence of a corrosion inhibitor with reasonable accuracy.