Research on Stress Corrosion Behavior of In-Service Pipeline in H2S Environment

Article Preview

Abstract:

Stress corrosion test of pressure vessels and piping in H2S environment has been explored extensively, but experimental research closed to the actual stress state of pipelines and the actual operating conditions, especially considered the combined effect of various factors is not common. Stress corrosion test simulated the actual operating conditions is taken in this paper. Four in-service pipes are researched as specimens and complex stress field is built by a specially designed loading device. Specimens are immersed in three different H2S concentration environments. The appearance and expansion of crack is observed regularly and the sensitivity of pipeline on stress corrosion is evaluated by metallographic examination. The result shows that: Intergranular corrosion, transgranular corrosion or micro-crack is not found in H2S corrosive solution (500×10-6, 800×10-6mg/L) after 2160 hours or in saturated H2S corrosive solution (greater than 2000×10-6mg/L) after 360 hours. A surface crack is found in H2S corrosive solution (500×10-6mg/L) after 720 hours and the expression for expansion rate of the crack during 2160 hours is a=16.835e0.0002h.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

1305-1312

Citation:

Online since:

February 2012

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2012 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

[1] CHEN Jinmei, JIN Yuhui, YANG Haitang. Risk Analysis of Pressure Pipeline in Service. Manufacturing Automation, 2010, 8: 95-97.

Google Scholar

[2] LIU Zhiwei, ZHAO Guiqin. Analysis of Pressure Piping Design Permit Rules and Counter Measures. Process Equipment & Piping, 2010, 47(2): 33-37.

Google Scholar

[3] LIU Zhan, WANG Zhiping , YU Shurong. A Study of the Pressure Pipeline Risk Management-Theory and Key Technology of Pressure Pipeline Risk Management. Petro-Chemical Equipment, 2007, 36(5): 1-5.

Google Scholar

[4] American Petroleum Institute. Risk Based Inspection. API 580. First Edition. 2002. 5.

Google Scholar

[5] GUO Bing , SHEN Gongtian, ZHANG Wanling. Application of RBI Technology in Atmospheric Storage Tanks. Pressure Vessel Technology, 2010, 4: 55-60.

Google Scholar

[6] XIANG Hanyin. Risk Based Inspection and Safety Insurance for Important Petrochemical Units. Pressure Vessel Technology, 2009, 26(5): 51-55, 59.

Google Scholar

[7] CHEN Xuedong, WANG Bing. Practice of RBI in Chinese Petrochemical Enterprises and Discussion about its Several Question. Pressure Vessel Technology, 2004, 21(8): 39-45.

Google Scholar

[8] Wu Qingyang. Application of Risk-based Inspection(RBI) in Zhenhai Refining & Chemical Company and Experience. Petrochemical Safety and Environmental Protection Technology, 2008, 24(3): 8-10.

Google Scholar

[9] LIU Zhiyong, LI Ming, LI Xiaogang. Stress Corrosion Crack of 16Mn Steel in Wet Sulfureted Hydrogen Environment. Journal of Chinese Society For Corrosion and Protection. 2006, 26(6): 360-364, 370.

Google Scholar

[10] NACE MR0175-97, Sulfide Stress Cracking Resistant Metallic Materials For Oilfield Equipment. (1997).

Google Scholar

[11] NACE TM0177-96, Laboratory Testing of Metals for Resistance to Specific Forms of Environmental Cracking in H2S Environments. (1996).

Google Scholar

[12] NACE TM0284-2003, Evaluation of Pipeline and Pressure Vessel Steels for Resistance to Hydrogen-Induced Cracking. (2003).

Google Scholar

[13] EFC Publications No. 16, Guidelines on Materials Requirements for Carbon and Low Alloy Steels for H2S-Containing Environments in Oil and Gas Production. Reprinted with Corrections. (1998).

DOI: 10.1201/9780429273858-6

Google Scholar