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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National Assoc. of Corrosion Engineers International
1996
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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 |
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Open Polar |
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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 |
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52 |
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4 |
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280 |
op_container_end_page |
294 |
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1766387935224004608 |