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      KCI등재 SCI SCIE SCOPUS

      Imitating Seasonal Temperature Fluctuations for the H2S Corrosion of 304L and 316L Austenitic Stainless Steels

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      https://www.riss.kr/link?id=A104267539

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      다국어 초록 (Multilingual Abstract)

      Temperature fluctuations are inevitable in sour oil and gas production. In this study, the H2S corrosion of 304L and 316L alloys was investigated at pH 3 and temperatures of 20-60 °C using DC and AC electrochemical techniques. Two-fold increases in the corrosion rates of both alloys were reported with increases in temperature to 60 °C. In the 304L alloy, the surface layer was observed to be 3% rougher and 34%thicker than that of the 316L alloy. The two alloys exhibited different corrosion behaviors in the temperature ranges of 20-40 °C and 40-60 °C. Although the 316L alloy revealed a greater corrosion resistance at the free potential condition, the passivation on the 304L alloy was significantly greater than that of the 316L alloy at 40 °C and 15 ppm H2S. The FeS2 and combined FeS2-MoS2 compounds contributed to the surface layer constituents in the 304L and 316L alloys, respectively. The increase in temperature kinetically provided more favorable conditions for FeS2 than MoS2 formation, i.e. it had a relatively constructive effect on the 304L alloy passivation.
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      Temperature fluctuations are inevitable in sour oil and gas production. In this study, the H2S corrosion of 304L and 316L alloys was investigated at pH 3 and temperatures of 20-60 °C using DC and AC electrochemical techniques. Two-fold increases in t...

      Temperature fluctuations are inevitable in sour oil and gas production. In this study, the H2S corrosion of 304L and 316L alloys was investigated at pH 3 and temperatures of 20-60 °C using DC and AC electrochemical techniques. Two-fold increases in the corrosion rates of both alloys were reported with increases in temperature to 60 °C. In the 304L alloy, the surface layer was observed to be 3% rougher and 34%thicker than that of the 316L alloy. The two alloys exhibited different corrosion behaviors in the temperature ranges of 20-40 °C and 40-60 °C. Although the 316L alloy revealed a greater corrosion resistance at the free potential condition, the passivation on the 304L alloy was significantly greater than that of the 316L alloy at 40 °C and 15 ppm H2S. The FeS2 and combined FeS2-MoS2 compounds contributed to the surface layer constituents in the 304L and 316L alloys, respectively. The increase in temperature kinetically provided more favorable conditions for FeS2 than MoS2 formation, i.e. it had a relatively constructive effect on the 304L alloy passivation.

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      참고문헌 (Reference)

      1 X. Liu, 66 : 161-, 2009

      2 B. Hirschorna, 55 : 6218-, 2010

      3 B. Beverskog, 55 : 1077-, 1999

      4 X. Cheng, 41 : 773-, 1999

      5 X. Cheng, 42 : 299-, 2000

      6 S. J. Yuan, 49 : 1276-, 2007

      7 Z. F. Yin, 51 : 1702-, 2009

      8 H. Ma, 42 : 1669-, 2000

      9 H. Ma, 451 : 11-, 1998

      10 C. Ren, 93 : 305-, 2005

      1 X. Liu, 66 : 161-, 2009

      2 B. Hirschorna, 55 : 6218-, 2010

      3 B. Beverskog, 55 : 1077-, 1999

      4 X. Cheng, 41 : 773-, 1999

      5 X. Cheng, 42 : 299-, 2000

      6 S. J. Yuan, 49 : 1276-, 2007

      7 Z. F. Yin, 51 : 1702-, 2009

      8 H. Ma, 42 : 1669-, 2000

      9 H. Ma, 451 : 11-, 1998

      10 C. Ren, 93 : 305-, 2005

      11 H. H. Huang, 58 : 177-, 1999

      12 J. Aali, 50 : 161-, 2006

      13 Y. Shirvany, 73 : 156-, 2010

      14 K. Mahdi, 61 : 116-, 2008

      15 G. Zhu, 71 : 30-, 2010

      16 M. S. H. Bader, 201 : 121-, 2006

      17 M. S. H. Bader, 55 : 93-, 2007

      18 J. Klein, 40 : 297-, 1994

      19 A. Davoodi, 43 : 399-, 2011

      20 C. C. Silva, 59 : 219-, 2007

      21 K. L. Ding, 35 : 401-, 2007

      22 M. Mohsen-Nia, 12 : 127-, 1994

      23 P. Mougin, 58 : 413-, 2007

      24 M. S. H. Bader, 201 : 100-, 2006

      25 M. El-Said, 249 : 748-, 2009

      26 H. R. Khatami, 71 : 13-, 2010

      27 T. Chevreau, 26 : 269-, 1990

      28 M. Salman, 55 : 48-, 2007

      29 X. M. Dong, 45 : 181-, 2010

      30 O. Karpash, 71 : 133-, 2010

      31 S. Nesic, 49 : 4308-, 2007

      32 J. J. Carroll, "Proc. 1st Annual Gas Processing Symp" Elsevier 276-, 2009

      33 W. Sun, "NACE proceedings" 2007

      34 W. Sun, "NACE proceedings" 2006

      35 K. L. J. Lee, "NACE proceedings" 2005

      36 I. Puigdomenech, "Medusa, Chemical Equilibrium Diagrams" Royal Institute of Technology, Department of Chemistry 2010

      37 A. L. Kohl, "Liquid Phase Oxidation Processes for Hydrogen Sulfide Removal, In Gas Purification, 5th ed" Gulf Professional Publishing 731-865, 1997

      38 S. Eliassen, "Guidelines on Materials Requirements for Carbon and Low Alloy Steels for H2S-Containing Environments in Oil and Gas Production, European Federation of Corrosion Publications, No. 16, 3rd ed" Maney Materials Science 2009

      39 A. L. Kohl, "Gas Purification, 5th ed" Gulf Publishing Company 1997

      40 M. E. Orazem, "Electrochemical Impedance Spectroscopy" John Wiley & Sons, Inc 2008

      41 L. Smith, "Corrosion Resistant Alloys for Oil and Gas Production: Guidance on General Requirements and Test Methods for H2S, In European Federation of Corrosion Publications, No. 17. 2nd ed" Maney Materials Science 1-19, 2002

      42 P. Marcus, "Corrosion Mechanisms in Theory and Practice 3rd ed" CRC Press 2011

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