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GROWTH BEHAVIOR AND MECHANISM OF STRESS CORROSION CRACKS OF X80 PIPELINE STEEL IN SIMULATED YINGTAN SOIL SOLUTION |
Zhiyong LIU1,2( ),Zongshu LI1,2,Xiaolin ZHAN1,2,Wenzhu HUANGFU1,2,Cuiwei DU1,2,Xiaogang LI1,2,3 |
1) Corrosion and Protection Center, University of Science and Technology Beijing, Beijing 100083, China. 2) Key Laboratory for Corrosion and Protection (MOE), Institute for Advanced Materials and Technology, University of Science and Technology Beijing, Beijing 100083, China. 3) Ningbo Institute of Material Technology & Engineering, Chinese Academy of Sciences, Ningbo 315201, China; |
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Cite this article:
Zhiyong LIU,Zongshu LI,Xiaolin ZHAN,Wenzhu HUANGFU,Cuiwei DU,Xiaogang LI. GROWTH BEHAVIOR AND MECHANISM OF STRESS CORROSION CRACKS OF X80 PIPELINE STEEL IN SIMULATED YINGTAN SOIL SOLUTION. Acta Metall Sin, 2016, 52(8): 965-972.
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Abstract Stress corrosion cracking (SCC) in soil environments is one of the major failure and accident causes for oil and gas pipelines, which have induced hundreds of damages all over the world, resulting in serious economic losses and casualties. Previous study showed that acidic soil environments in Southeast of China are highly sensitive to SCC of pipeline steels. However, there is less research on the behavior and mechanism of growth behavior of SCC in this environment up to date. SCC behavior and mechanism of X80 pipeline steel in the simulated solution of Yingtan in China was investigated with electrochemical polarization curves, EIS, slow-rate-loading crack-growth test and SEM. Results showed that the applied polarization potential played an important role in SCC growth behavior and mechanism of X80 pipeline steel in the simulated solution of the acid soil environment. With the decreasing of the applied potential, the crack propagation rate increased constantly. In comparison to the crack propagation at the open circuit potential, the cracks extended faster in the initial stage of crack propagation when the applied potential was -850 mV; nevertheless, in the rapid propagation stage, the rate of the propagation was magnified with the application of -1200 mV potential. In addition, the crack propagation mode varied with applied potentials: it was mixed-controlled by both anodic dissolution (AD) and hydrogen embrittlement (HE) when the applied potential was more positive than -930 mV, and only in control of HE when the potential was less than -930 mV.
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Received: 27 October 2015
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Fund: Supported by National Basic Research Program of China (No.2014CB643300), National Natural Science Foundation of China (Nos.51371036, 51131001 and 51471034) and Beijing Higher Education Young Elite Teacher Project |
[1] | Cheng Y F.Electrochim Acta, 2007; 52: 2661 | [2] | Liu Z Y, Cui Z Y, Li X G, Du C W, Xing Y Y.Electrochem Commun, 2014; 48: 127 | [3] | Liu Z Y, Li X G, Du C W, Chen X, Liang P, Zhang L.Oil Gas Storage Transp, 2008; 27(4): 34 | [3] | (刘智勇, 李晓刚, 杜翠薇, 陈旭, 梁平, 张亮. 油气储运, 2008; 27(4): 34) | [4] | Liu Z Y, Wang C P, Du C W, Li X G.Acta Metall Sin, 2011; 47: 1434 | [4] | (刘智勇, 王长朋, 杜翠薇, 李晓刚. 金属学报, 2011; 47: 1434) | [5] | Zhou J L, Li X G, Du C W, Li Y L, Li T, Pan Y.Acta Metall Sin, 2010; 46: 251 | [5] | (周建龙, 李晓刚, 杜翠薇, 李云玲, 李涛, 潘莹. 金属学报, 2010; 46: 251) | [6] | Kang Y W, Chen W X, Kania R, Boven G V, Worthingham R.Corros Sci, 2011; 53: 968 | [7] | Liu Z Y, Li X G, Du C W, Cheng Y F.Corros Sci, 2009; 51: 2863 | [8] | Nanfredi C, Otegui J L.Eng Fail Anal, 2002; 9: 495 | [9] | Arafin M A, Szpunar J A.Corros Sci, 2009; 51: 119 | [10] | Jack T R, Erno B, Krist K.Corrosion, 2000; 362: 10 | [11] | Li B T, Song F M, Gao M, Elboujdaini M.Corros Sci, 2010; 52: 4064 | [12] | Li M C, Cheng F M.Electrochim Acta, 2008; 53: 2831 | [13] | Song F M..Corros Sci, 2009; 51: 2657 | [14] | Li Q, Liu Z Y, Du C W, Li X G, Liu R K.Surf Technol, 2015; 44(3): 31 | [14] | (李琼, 刘智勇, 杜翠薇, 李晓刚, 刘然克. 表面技术, 2015; 44(3): 31) | [15] | Gonzalez-Rodriguez J G, Casales M, Salinas-Bravo V M, Albarran J L, Martinez L.Corrosion, 2002; 58: 584 | [16] | Javidi M, Hore S B.Corros Sci, 2014; 80: 213 | [17] | Liu Z Y, Li X G, Cheng Y F.Corros Sci, 2012; 55: 54 | [18] | He D X, Chen W, Luo J L.Corrosion, 2004; 60: 778 | [19] | Parkins R N, Blanchard W K Jr,Delanty B S.Corrosion, 1994; 50: 394 | [20] | Park J J, Pyun S I, Na K H, Lee S M, Kho Y T.Corrosion, 2002; 58: 329 | [21] | Yan M C, Sun C, Xu J, Wu T Q, Yang S, Ke W.Corros Sci, 2015; 93: 27 | [22] | Cheng Y F, Niu L.Electrochem Commun, 2007; 9: 558 | [23] | Cao C N.Principles of Electrochemistry of Corrosion. 2nd Ed.,Beijing: Chemical Industry Press, 2003: 111 | [23] | (曹楚南. 腐蚀电化学原理. 第二版, 北京: 北京化学工业出版社, 2003: 111) | [24] | Pan B W, Peng X, Chu W Y.Mater Sci Eng, 2006; A434: 76 | [25] | He D X, Chen W, Luo J L.Corrosion, 2004; 8: 778 | [26] | Chen W, King F, Vokes E D.Corrosion, 2002; 3: 267 | [27] | Liu Z Y, Zhai G L, Du C W, Li X G.Acta Metall Sin, 2008; 44: 209 | [27] | (刘智勇, 翟国丽, 杜翠薇, 李晓刚. 金属学报, 2008; 44: 209) | [28] | Xu C M, Huo C Y, Xiong Q R, Shi K, Yang A M, Zhou Y.Mater Mech Eng, 2009; 33(5): 29 | [28] | (胥聪敏, 霍春勇, 熊庆人, 石凯, 杨爱民, 周勇. 机械工程材料, 2009; 33(5): 29) | [29] | Lu B T, Luo J L.Corrosion, 2006; 26: 129 | [30] | Liu Z Y, Lu L, Huang Y Z, Du C W, Li X G.Corrosion, 2014; 70: 678 | [31] | Fan L, Liu Z Y, Du C W, Li X G.Acta Metall Sin, 2013; 49: 689 | [31] | (范林, 刘智勇, 杜翠薇, 李晓刚. 金属学报, 2013; 49: 689) | [32] | Wang X Z, Liu Z Y, Ge X, Zhan X L, Du C W, Li X G.Corrosion, 2014; 70: 872 |
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