Study on Corrosion Behavior of the 304 Stainless Steel in the Heavy Oil with High Salt, High Sulfur and High Acid Value

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The uniform corrosion and localized corrosion of 304 stainless steel in heavy oil with high salt, high sulfur and high acid value were researched by weight loss method and electrochemical method. The corrosion morphology of samples with and without corrosion product films and the compositions of the corrosion product films were observed using SEM and EDS. The results show that the 304 stainless steel is inapplicable to the refinery equipment of this heavy oil because of the severe local corrosion even if the uniform corrosion rate is as low as 0.0107mm/a. The salt corrosion and sulfur corrosion occur on the local surface of 304 stainless steel because of the chloride ion formed by hydrolysis of salt in the small emulsifying water. The water soluble iron naphthenate produced by chemical reaction between naphthenic and ferrous sulfides impel the local corrosion of the 304 stainless steel.

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271-275

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December 2012

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] Babaian-Kibala E, Petersen P R, Humphries M J. Corrosion by naphthenic acids in crude oils[J]. Division of petroleum chemistry, 1998, 3: 106.

Google Scholar

[2] J. Skippens, D. Johnson, R. Davies. Evaluation of the economics for processing of naphthenic crudes. International conference for corrosion in refinery petrochemical and power generation plants. Venic 18-19 May, (2000).

Google Scholar

[3] Zhang Deyi acid-sulfur crude oil processing technology progress [J]. Refining technology and engineering, 2012, 42 (1) : 1.

Google Scholar

[4] Long Wei Chan, Liu Jianping, Li Hua, high-sulfur, high acid heavy crude optimize procurement and processing [J] Petroleum Processing and Petrochemicals, 2009, 40 (2) : 49.

Google Scholar

[5] Gao Hui, Zhu Jianhua, Chen Suxia. The crude metal removal agents of various kinds of steel corrosive evaluation [J]. Petrochemical Corrosion and protection, 2006, 23 (3) : 15.

Google Scholar

[6] Liu Wei, Liu Hongfu low-acid crude oil processing sour crude distillation unit pipeline design selection [J]. Refining Technology and Engineering, 2003, 33 (9) : 43.

Google Scholar

[7] Peng Jin processing sour crude oil pipe selection optimization [J]. Petrochemical Corrosion and protection, 1999, 16 (3): 46.

Google Scholar

[8] Lu Shiying stainless steel [M] Beijing: Atomic Energy Press, (1995).

Google Scholar

[9] Cao Chu-Nan, Zhang Jianqing Electrochemical impedance spectroscopy Introduction [M] Beijing: Science and Technology Press, (2002).

Google Scholar

[10] Cao Chu-Nan, Wang Jia, Lin Hai-chloride ions on the passive metal electrode impedance spectrum [J]. Chinese Society for Corrosion and protection, 1989, 9 (4) : 261.

Google Scholar

[11] E. Slavcheva, B. Shone, A. Turnbull. Review of naphthenic acid corrosion in oil refining[J]. British corrosion journal, 1999, 34(2): 125.

DOI: 10.1179/000705999101500761

Google Scholar

[12] P. Waldner A.D. Pellon. Thermodynamic modeling of the Fe-S system[J]. Journal of phase equilibria and diffusion, 2005, 26(1): 23.

Google Scholar

[13] T Ohmi, Y Nakagawa, M Nakamura. Formation of chromium oxide on 316L austenitic stainless steel[J]. Journal of vacuum science & technology A: vacuum, surfaces, and films, 1996, 14(4): 2505.

DOI: 10.1116/1.580010

Google Scholar