A Mechanistic Model for Carbon Dioxide Corrosion of Mild Steel in the Presence of Protective Iron Carbonate Films—Part 1: Theory and Verification

By M. Nordsveen, S. Nesic, R. Nyborg, A. Stangeland. 2003

513 citations recorded by the source corpus.

Subfields: Civil and Structural Engineering, Environmental Engineering, Materials Chemistry

View Paper: https://www.semanticscholar.org/paper/45b8d9a8ba7a92fa9e6b587a5de0c86c4fbc93d8

How researchers see this paper

The researchers whose trusted networks rank it highest, strongest advocate first. Every researcher gets a different order.

In Civil and Structural Engineering

1. C. Noubactep
2. M. Singer
3. Aria Kahyarian
4. S. Nesic

In Environmental Engineering

1. C. Noubactep
2. S. Nesic

In Materials Chemistry

1. C. Noubactep
2. M. Singer
3. Aria Kahyarian
4. R. Barker
5. Anne Neville
6. Y. Hua
7. S. Nesic

Citations in the corpus

• The fundamental mechanism of aqueous contaminant removal by metallic iron (2010, background): “…No. 5 October 2010 665 • Co-precipitated contaminants are not likely to be released into the environment unless iron oxides are dissolved (Stipp et al., 2002; Noubactep et al., 2003; Noubactep et al., 2006a; Noubactep et al., 2006b; Noubactep, 2009c; Noubactep et al., 2009a; Ghauch et al., 2010a).”
• Modeling of uniform CO2 corrosion of mild steel in gas transportation systems: A review (2016, methodology): “The key point for this discussion is that this model was directly adapted from the mechanistic CO2 corrosion approach developed by Nordsveen (2003) and Nesic et al. (Ne si c and Lee, 2003; Ne si c et al., 2003, 2001).”
• Corrosion inhibition of mild steel by ethylamino imidazoline derivative in CO2-saturated solution (2009, unknown): “However, significant progress has been achieved in understanding the mechanism of CO2 corrosion in the oil and gas industry [7,12–18], but an understanding of its inhibition mechanism and the kinetics of the inhibition process necessary to quantify formulations that will provide a desirable level of”
• Internal corrosion of carbon steel pipelines for dense-phase CO2 transport in carbon capture and storage (CCS) – a review (2017, background): “0 MPa) and has been an active area of study for the past 50 years.([37-43]) However, less research has been afforded to high pressure CO2 corrosion where CO2 is the dominant phase([44]), especially in conditions”
• Evolution of dissolution processes at the interface of carbon steel corroding in a CO2 environment studied by EIS (2010, background): “This barrier influences the transport of the corrosive species presented in the electrolyte [3].”