An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions

A predictive model was developed for uniform carbon dioxide (CO) corrosion, based on modeling of individual electrochemical reactions in a water-CO system. The model takes into account the electrochemical reactions of hydrogen ion (H) reduction, carbonic acid (HCO) reduction, direct water reduction,...

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Published in:CORROSION
Main Authors: Nesic, S., Postlethwaite, J., Olsen, S.
Format: Article in Journal/Newspaper
Language:English
Published: National Assoc. of Corrosion Engineers International 1996
Subjects:
pH
Online Access:https://espace.library.uq.edu.au/view/UQ:691945
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spelling ftunivqespace:oai:espace.library.uq.edu.au:UQ:691945 2023-05-15T15:52:50+02:00 An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions Nesic, S. Postlethwaite, J. Olsen, S. 1996-04-01 https://espace.library.uq.edu.au/view/UQ:691945 eng eng National Assoc. of Corrosion Engineers International doi:10.5006/1.3293640 issn:0010-9312 Aqueous solutions Carbon dioxide corrosion Carbon steel Films and film formation Flow Mass transfer Modeling pH Temperature Uniform corrosion Weight loss 1500 Chemical Engineering 1600 Chemistry 2500 Materials Science Journal Article 1996 ftunivqespace https://doi.org/10.5006/1.3293640 2020-11-24T02:41:02Z A predictive model was developed for uniform carbon dioxide (CO) corrosion, based on modeling of individual electrochemical reactions in a water-CO system. The model takes into account the electrochemical reactions of hydrogen ion (H) reduction, carbonic acid (HCO) reduction, direct water reduction, oxygen reduction, and anodic dissolution of iron. The required electrochemical parameters (e.g., exchange current densities and Tafel slopes) for different reactions were determined from experiments conducted in glass cells. The corrosion process was monitored using polarization resistance, potentiodynamic sweep, electrochemical impedance, and weight-loss measurements. The model was calibrated for two mild steels over a range of parameters: temperature (t) = 20°C to 80°C, pH = 3 to 6, partial pressure of CO (P) = 0 bar to 1 bar (0 κPa to 100 κPa), and ω = 0 rpm to 5,000 rpm (ν = 0 m/s to 2.5 m/s). The model was applicable for uniform corrosion with no protective films present. Performance of the model was validated by comparing predictions to results from independent loop experiments. Predictions also were compared to those of other CO corrosion prediction models. Compared to the previous largely empirical models, the model gave a clearer picture of the corrosion mechanisms by considering the effects of pH, temperature, and solution flow rate on the participating anodic and cathodic reactions. Article in Journal/Newspaper Carbonic acid The University of Queensland: UQ eSpace CORROSION 52 4 280 294
institution Open Polar
collection The University of Queensland: UQ eSpace
op_collection_id ftunivqespace
language English
topic Aqueous solutions
Carbon dioxide corrosion
Carbon steel
Films and film formation
Flow
Mass transfer
Modeling
pH
Temperature
Uniform corrosion
Weight loss
1500 Chemical Engineering
1600 Chemistry
2500 Materials Science
spellingShingle Aqueous solutions
Carbon dioxide corrosion
Carbon steel
Films and film formation
Flow
Mass transfer
Modeling
pH
Temperature
Uniform corrosion
Weight loss
1500 Chemical Engineering
1600 Chemistry
2500 Materials Science
Nesic, S.
Postlethwaite, J.
Olsen, S.
An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions
topic_facet Aqueous solutions
Carbon dioxide corrosion
Carbon steel
Films and film formation
Flow
Mass transfer
Modeling
pH
Temperature
Uniform corrosion
Weight loss
1500 Chemical Engineering
1600 Chemistry
2500 Materials Science
description A predictive model was developed for uniform carbon dioxide (CO) corrosion, based on modeling of individual electrochemical reactions in a water-CO system. The model takes into account the electrochemical reactions of hydrogen ion (H) reduction, carbonic acid (HCO) reduction, direct water reduction, oxygen reduction, and anodic dissolution of iron. The required electrochemical parameters (e.g., exchange current densities and Tafel slopes) for different reactions were determined from experiments conducted in glass cells. The corrosion process was monitored using polarization resistance, potentiodynamic sweep, electrochemical impedance, and weight-loss measurements. The model was calibrated for two mild steels over a range of parameters: temperature (t) = 20°C to 80°C, pH = 3 to 6, partial pressure of CO (P) = 0 bar to 1 bar (0 κPa to 100 κPa), and ω = 0 rpm to 5,000 rpm (ν = 0 m/s to 2.5 m/s). The model was applicable for uniform corrosion with no protective films present. Performance of the model was validated by comparing predictions to results from independent loop experiments. Predictions also were compared to those of other CO corrosion prediction models. Compared to the previous largely empirical models, the model gave a clearer picture of the corrosion mechanisms by considering the effects of pH, temperature, and solution flow rate on the participating anodic and cathodic reactions.
format Article in Journal/Newspaper
author Nesic, S.
Postlethwaite, J.
Olsen, S.
author_facet Nesic, S.
Postlethwaite, J.
Olsen, S.
author_sort Nesic, S.
title An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions
title_short An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions
title_full An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions
title_fullStr An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions
title_full_unstemmed An Electrochemical Model for Prediction of Corrosion of Mild Steel in Aqueous Carbon Dioxide Solutions
title_sort electrochemical model for prediction of corrosion of mild steel in aqueous carbon dioxide solutions
publisher National Assoc. of Corrosion Engineers International
publishDate 1996
url https://espace.library.uq.edu.au/view/UQ:691945
genre Carbonic acid
genre_facet Carbonic acid
op_relation doi:10.5006/1.3293640
issn:0010-9312
op_doi https://doi.org/10.5006/1.3293640
container_title CORROSION
container_volume 52
container_issue 4
container_start_page 280
op_container_end_page 294
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