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Volume 25 Issue 7
Jul.  2018
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文章导航 >  矿物冶金与材料学报（英文）  > 2018  >  25(7): 779-787
Yong Li, Min-dong Chen, Jian-kuan Li, Long-fei Song, Xin Zhang,  and Zhi-yong Liu, Flow-accelerated corrosion behavior of 13Cr stainless steel in a wet gas environment containing CO2, Int. J. Miner. Metall. Mater., 25(2018), No. 7, pp. 779-787. https://doi.org/10.1007/s12613-018-1626-3
Cite this article as:
Yong Li, Min-dong Chen, Jian-kuan Li, Long-fei Song, Xin Zhang,  and Zhi-yong Liu, Flow-accelerated corrosion behavior of 13Cr stainless steel in a wet gas environment containing CO2, Int. J. Miner. Metall. Mater., 25(2018), No. 7, pp. 779-787. https://doi.org/10.1007/s12613-018-1626-3
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研究论文

Flow-accelerated corrosion behavior of 13Cr stainless steel in a wet gas environment containing CO2

  • Corrosion and Protection Centre, Key Laboratory for Corrosion and Protection (MOE) National Environmental Corrosion Platform (NECP), University of Science and Technology Beijing, Beijing 100083, China

  • Nuclear and Radiation Safety Center, Ministry of Environmental Protection of P.R. China, Beijing 100082, China

  • 通讯作者:

    Zhi-yong Liu    E-mail: liuzhiyong7804@126.com

  • This work investigated the flow-accelerated corrosion (FAC) behavior of 13Cr in a wet CO2-containing environment at different flowing gas velocities and impinging angles, with the natural-gas pipeline environment simulated by a self-assembled impingement jet system. Surface morphology determination, electrochemical measurements, and hydromechanics numerical analysis were carried out to study the FAC behavior. The results demonstrate that pitting corrosion was the primary mode of corrosion in 13Cr stainless steel. High-flow-rate gas destroyed the passive film and decreased the pitting potential, resulting in more serious corrosion. The corrosion degree with various impact angles showed the following order: 90° > 60° > 45°. The shear force and the electrolyte from the flowing gas were concluded to be the determinant factors of FAC, whereas the shear force was the main factor responsible for destroying the passive film.
    • Research Article

    Flow-accelerated corrosion behavior of 13Cr stainless steel in a wet gas environment containing CO2

    + Author Affiliations
      Abstract
    • This work investigated the flow-accelerated corrosion (FAC) behavior of 13Cr in a wet CO2-containing environment at different flowing gas velocities and impinging angles, with the natural-gas pipeline environment simulated by a self-assembled impingement jet system. Surface morphology determination, electrochemical measurements, and hydromechanics numerical analysis were carried out to study the FAC behavior. The results demonstrate that pitting corrosion was the primary mode of corrosion in 13Cr stainless steel. High-flow-rate gas destroyed the passive film and decreased the pitting potential, resulting in more serious corrosion. The corrosion degree with various impact angles showed the following order: 90° > 60° > 45°. The shear force and the electrolyte from the flowing gas were concluded to be the determinant factors of FAC, whereas the shear force was the main factor responsible for destroying the passive film.
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    • [1]
      X.G. Li, D.W. Zhang, Z.Y. Liu, Z. Li, C.W. Du, and C.F. Dong, Materials science: share corrosion data, Nature, 527(2015), No. 7579, p. 441.
      [2]
      S. Nešić, Key issues related to modelling of internal corrosion of oil and gas pipelines—a review, Corros. Sci., 49(2007), No. 12, p. 4308.
      [3]
      J.W. Yang, H2S/CO2 corrosion of X60 pipeline steel in wet gas and solution, Acta Metall. Sin., 44(2008), No. 11, p. 1366.
      [4]
      S.S. Rajahram, T.J. Harvey, and R.J.K. Wood, Erosion-corrosion resistance of engineering materials in various test conditions, Wear, 267(2009), No. 1-4, p. 244.
      [5]
      K. Najmi, B.S. McLaury, S.A. Shirazi, and S. Cremaschi, Experimental study of low concentration sand transport in wet gas flow regime in horizontal pipes, J. Nat. Gas Sci. Eng., 24(2015), p. 80.
      [6]
      P.B. Machado, J.G.M. Monteiro, J.L. Medeiros, H.D. Epsom, and O.Q.F. Araujo, Supersonic separation in onshore natural gas dew point plant, J. Nat. Gas Sci. Eng., 6(2012), p. 43.
      [7]
      L.T. Wang, Y.Y. Xing, Z.Y. Liu, D.W. Zhang, C.W. Du, and X.G. Li, Erosion-corrosion behavior of 2205 duplex stainless steel in wet gas environments, J. Nat. Gas Sci. Eng., 35(2016), p. 928.
      [8]
      X.M. Hu and A. Neville, CO2 erosion-corrosion of pipeline steel (API X65) in oil and gas conditions—a systematic approach, Wear, 267(2009), No. 11, p. 2027.
      [9]
      A. Kahyarian, M. Singer, and S. Nesic, Modeling of uniform CO2 corrosion of mild steel in gas transportation systems: a review, J. Nat. Gas Sci. Eng., 29(2016), p. 530.
      [10]
      M. Bagheri, A. Alamdari, and M. Davoudi, Quantitative risk assessment of sour gas transmission pipelines using CFD, J. Nat. Gas Sci. Eng., 31(2016), p. 108.
      [11]
      L. Giourntas, T. Hodgkiess, and A.M. Galloway, Comparative study of erosion-corrosion performance on a range of stainless steels, Wear, 332-333(2015), p. 1051.
      [12]
      D.A. López, T. Pérez, and S.N. Simison, The influence of microstructure and chemical composition of carbon and low alloy steels in CO2 corrosion. A state-of-the-art appraisal, Mater. Des., 24(2003), No. 8, p. 561.
      [13]
      G.A. Zhang and Y.F. Cheng, Electrochemical corrosion of X65 pipe steel in oil/water emulsion, Corros. Sci., 51(2009), No. 4, p. 901.
      [14]
      M.A. Islam and Z.N. Farhat, The synergistic effect between erosion and corrosion of API pipeline in CO2 and saline medium, Tribol. Int., 68(2013), p. 26.
      [15]
      R.J.K. Wood, J.C. Walker, T.J. Harvey, S. Wang, and S.S. Rajahram, Influence of microstructure on the erosion and erosion-corrosion characteristics of 316 stainless steel, Wear, 306(2013), No. 1-2, p. 254.
      [16]
      E. Mahdi, A. Rauf, and E.O. Eltai, Effect of temperature and erosion on pitting corrosion of X100 steel in aqueous silica slurries containing bicarbonate and chloride content, Corros. Sci., 83(2014), p. 48.
      [17]
      Y.L. Zhao, F. Zhou, J. Yao, S.G. Dong, and N. Li, Erosion-corrosion behavior and corrosion resistance of AISI 316 stainless steel in flow jet impingement, Wear, 328-329(2015), p. 464.
      [18]
      G.A. Zhang, L.Y. Xu, and Y.F. Cheng, Investigation of erosion-corrosion of 3003 aluminum alloy in ethylene glycol-water solution by impingement jet system, Corros. Sci., 51(2009), No. 2, p. 283.
      [19]
      W.M. Zhao, C. Wang, T.M. Zhang, M. Yang, B. Han, and A. Neville, Effects of laser surface melting on erosion-corrosion of X65 steel in liquid-solid jet impingement conditions, Wear, 362-363(2016), p. 39.
      [20]
      G.A. Zhang, L. Zeng, H.L. Huang, and X.P. Guo, A study of flow accelerated corrosion at elbow of carbon steel pipeline by array electrode and computational fluid dynamics simulation, Corros. Sci., 77(2013), p. 334.
      [21]
      S. Papavinasam, R. Revie, M. Attard, A. Demoz, and K. Michaelian, Comparison of laboratory methodologies to evaluate corrosion inhibitors for oil and gas pipelines, Corrosion, 59(2003), No. 10, p. 897.
      [22]
      X. Jiang, Y.G. Zheng, and W. Ke, Effect of flow velocity and entrained sand on inhibition performances of two inhibitors for CO2 corrosion of N80 steel in 3% NaCl solution, Corros. Sci., 47(2005), No. 11, p. 2636.
      [23]
      A.H. Hosseinloo, F.F. Yap, and L.Y. Lim, Design and analysis of shock and random vibration isolation system for a discrete model of submerged jet impingement cooling system, J. Vib. Control, 21(2015), No. 3, p. 468.
      [24]
      H. Luo, C.F. Dong, X.G. Li, and K. Xiao, The electrochemical behaviour of 2205 duplex stainless steel in alkaline solutions with different pH in the presence of chloride, Electrochim. Acta, 64(2012), p. 211.
      [25]
      X.F. Wang, Z.J. Dong, Y.J. Liang, Z.H. Zhang, and C.F. Chen, Development of economic steels with low Cr content for anti-corrosion oil tube, Corros. Sci. Protect. Technol., 18(2006), No. 6, p. 436.
      [26]
      H. Takabe and M. Ueda, The relationship between CO2 corrosion resistance and corrosion products structure on carbon and low Cr bearing steels, Corros. Eng., 56(2007), No. 11, p. 514.
      [27]
      G.A. Zhang and Y.F. Cheng, Electrochemical characterization and computational fluid dynamics simulation of flow-accelerated corrosion of X65 steel in a CO2-saturated oilfield formation water, Corros. Sci. 52(2010), No. 8, p. 2716.
      [28]
      K. Stewartson, Mechanics of Fluids, Nature, 272(1978), No. 5648, p. 109.
      [29]
      B.S. Massey and J. Ward-Smith, Mechanics of Fluids, CRC Press, Boca Raton, 1998, p. 36.
      [30]
      B.R. Munson, D.F. Young, and T.H. Okiishi, Fundamentals of Fluid Mechanics, 3rd Ed. Wiley, New York, 1990, p. 16.
      [31]
      M. Metikoš-Huković, I. Škugor, Z. Grubač, and R. Babić, Complexities of corrosion behaviour of copper-nickel alloys under liquid impingement conditions in saline water, Electrochim. Acta, 55(2010), No. 9, p. 3123.
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