This study investigates the corrosion behavior of three stainless steel grades at two H2SO4 concentrations, namely 1 wt% and 10 wt%, with varying NaCl concentrations in the range from 500 mg/L to 10,000 mg/L. Dissociation of sulfuric acid yields the hydrogen (H+) and sulfate () ions, the former of which lowers the pH value of a solution while the latter increases the concentration of sulfate ions that act as a corrosion inhibitor. The equilibrium chemistry of the solutions was defined at the test temperatures of 22°C, 50°C, 90°C, and 130°C, and correlated with the observations on the electrochemical and microstructural examination of the materials. The results showed clear differences in the main corrosion form between the two H2SO4 concentrations. In 1 wt% H2SO4, pitting was the major form of corrosion attack in the presence of chlorides, whereas uniform corrosion dominated in 10 wt% H2SO4. The pitting corrosion tendency for the three stainless steel grades under various test conditions was consistent, but there were differences in their resistance to uniform corrosion. The chloride-to-sulfate activity ratio,
, was found to be the key parameter in defining the occurrence of pitting corrosion for all three alloys. In H2SO4-NaCl systems, no pitting occurred at the activity ratio
below 10, with higher values inducing pitting attack, particularly in 1 wt% H2SO4. The described novel results are presented and discussed in this paper.
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1 October 2022
Research Article|
August 02 2022
Corrosion of Stainless Steels S31603, S31655, and S32101 in Sulfuric Acid Solutions: Effects of Concentration, Chlorides, and Temperature
E. Huttunen-Saarivirta;
E. Huttunen-Saarivirta
‡
*VTT Technical Research Centre of Finland Ltd., P.O. Box 1000, FI-02044 VTT, Finland.
‡Corresponding author. E-mail: [email protected].
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E. Isotahdon;
E. Isotahdon
*VTT Technical Research Centre of Finland Ltd., P.O. Box 1000, FI-02044 VTT, Finland.
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M. Lindgren;
M. Lindgren
**Metso Outotec Research Center, P.O. Box 69, FI-28101 Pori, Finland.
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A. Mardoukhi;
A. Mardoukhi
**Metso Outotec Research Center, P.O. Box 69, FI-28101 Pori, Finland.
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P. Mocnik;
P. Mocnik
***ZAG Slovenian National Building and Civil Engineering Institute, Dimičeva ulica 12, Ljubljana, SI 1000, Slovenia.
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T. Kosec;
T. Kosec
***ZAG Slovenian National Building and Civil Engineering Institute, Dimičeva ulica 12, Ljubljana, SI 1000, Slovenia.
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J.B. Jorcin;
J.B. Jorcin
****Tecnalia, Parque Cientifico y Tecnologico de Bizkaia, Derio, Spain.
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S. Hägg Mameng;
S. Hägg Mameng
*****Outokumpu Stainless AB, Box 74, SE-77422 Avesta, Sweden.
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Y. El Ouazari;
Y. El Ouazari
*****Outokumpu Stainless AB, Box 74, SE-77422 Avesta, Sweden.
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L. Wegrelius
L. Wegrelius
*****Outokumpu Stainless AB, Box 74, SE-77422 Avesta, Sweden.
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‡Corresponding author. E-mail: [email protected].
Online ISSN: 1938-159X
Print ISSN: 0010-9312
© 2022, AMPP
2022
CORROSION (2022) 78 (10): 943–962.
Citation
E. Huttunen-Saarivirta, E. Isotahdon, M. Lindgren, A. Mardoukhi, P. Mocnik, T. Kosec, J.B. Jorcin, S. Hägg Mameng, Y. El Ouazari, L. Wegrelius; Corrosion of Stainless Steels S31603, S31655, and S32101 in Sulfuric Acid Solutions: Effects of Concentration, Chlorides, and Temperature. CORROSION 1 October 2022; 78 (10): 943–962. https://doi.org/10.5006/4122
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