期刊文献+

高温高压及醋酸环境中H_2S对油管钢CO_2腐蚀行为的影响 被引量:6

Effect of H_2S on CO_2 Corrosion of Oil Tube Steel in High Temperature and High Pressure Environments Containing Acetic Acid
在线阅读 下载PDF
导出
摘要 利用美国Cortest公司高温高压反应釜模拟高含硫油气田H2S/CO2及醋酸共存环境,在流动高矿化度饱和H2S/CO2介质中进行试验,辅以SEM、XRD、动电位扫描及交流阻抗等表面分析和电化学技术,探讨了高温高压及醋酸环境中H2S对油管钢CO2腐蚀行为的影响。结果表明:普通N80油管钢在单一CO2腐蚀速率较高,达到5.1mm/a,加入H2S后腐蚀速率明显受到抑制,降幅最大的点出现在H2S分压最小处,低至0.28mm/a,随着H2S分压的继续增大,腐蚀速率略有增加,但远低于单一CO2腐蚀速率。加入H2S后腐蚀产物以四方晶系的FeS(Mackinawite)为主,未出现FeCO3,腐蚀过程转变为H2S控制。试样的腐蚀形态以局部腐蚀为主,试样表面均出现了严重的点蚀,醋酸的存在增大了油管钢在H2S/CO2环境中产生局部腐蚀的倾向性。 Solution immersion environments containing HzS/CO2 and acetic acid were simulated in a high temperature and high pressure autoclave manufactured by UAS Cortest Company, and test was conducted in flowing H2S/CO2 medium with high salinity. The Effect of H2S on CO2 corrosion of oil tube steel were analyzed and discussed by the following electrochemistry technologies, such as SEM, XRD, dynamic potential scanning, AC impedance and etc. The results showed that the corrosion rate of N80 oil tube steel is very high, up to 5.1mm/a, when solution immersion environment contain only CO2 and acetic acid. However, with the addition of H2S, the corrosion rate is restrained obviously and the largest decreasing point is observed at the lowest partial pressure of l'i2S, down to 0.28 mm/a. With H_,S partial pressure increasing, the corrosion rate slightly increased, but is far lower than simplex CO2 corrosion rate. With the presence of H2S, the corrosion products are mainly FeS (Mackinawite), FeCO3 doesn't appear, and corrosion is controlled by H2S. The corrosion forms of samples are mainly localized corrosion, severe pitting presents on surface of samples, and exist of acetic acid promotes the tendency of pitting of oil tube steel in H2S/CO2 environment.
出处 《焊管》 2011年第10期9-15,共7页 Welded Pipe and Tube
关键词 油管钢 高温高压 H2S/CO2腐蚀 醋酸 点蚀 oil tube steel high temperature and high pressure HzS/CO2 corrosion acetic acid pitting
  • 相关文献

参考文献15

  • 1GRECO E C, WRIGHT W B. Corrosion of Iron in an H2S-CO2-H2O System[J].Corrosion, 1962(18): 119.
  • 2BONIS M, GIRGIS M, GOERZ K,et al. Weight Loss Corrosion with H2S: Using Past Operations for Designing Future Facilities [C]//Corrosion /06.Houston, TX:NACE International, 2006:122.
  • 3赵新伟,罗金恒,郑茂盛,李鹤林,张华.弥散型腐蚀损伤管道剩余寿命预测方法[J].石油学报,2006,27(1):119-123. 被引量:20
  • 4顾春元,狄勤丰,王掌洪.N80钢在地层水中的应力腐蚀行为研究[J].石油学报,2006,27(2):141-144. 被引量:17
  • 5DOMIZZI G, ANTERI G, OVEJERO-GARCIA J.Influence of Sulphur Content and Inclusion Distribution on Hydrogen Induced Blister Cracking in Pressure Vessel and Pipeline Steels[J] .Corrosion Science, 2001(43):325-339.
  • 6OMWEG G M, FRANKEL G S, BRUCE W A, et al. Performance of Welded High-strength Low-alloy Steels in Sour Environments[J] .Corrosion, 2003,59(7):640-653.
  • 7SARDISCO J B, WRIGHT W B, GRECO E C. CoITosion of Iron in an H2S-CO2-H2O System Corrosion Film Properties on Pure Iron[J].Corrosion, 1963,19( 10): 354-359.
  • 8REN C Q, LIU D X. Corrosion Behavior of Oil Tube Steel in Simulant Solution with Hydrogen Sulfide and Carbon Dioxide[J].Materials Chemistry and Physics,2005 (93): 305-309.
  • 9LEE K J. A Mechanistic Modeling of CO2 Corrosion of Mild Steel in the Presence of H2S [D].PhD Dissertation, Ohio University, 2004.
  • 10KVAREKVAL J, Nyborg R. Formation of Muhilayer Iron Sulfide Films During High Temperature COJH2S Corrosion of Carbon Steel [ C ]//Corrosion / 03. Houston, Texas: NACE International, 2003:630.

二级参考文献19

  • 1郝文森,韩万学,王宙.1000m^3N-TuF50钢制球罐裂纹形成分析[J].石油学报,1997,18(1):129-132. 被引量:2
  • 2赵新伟 路民旭 白真权.在役输气管道腐蚀特点及腐蚀类型调查[J].石油专用管,1998,6(2):47-51,62.
  • 3Kiefner J F,Maxey W A,Eiber R J,et al.Failure stress levels of flaws in pressurized cylinders[M]//Progress in flaw growth and fracture toughness testing.ASTM STP 536,1973:461-481.
  • 4Maxey W A,Kiefner J F,Eiber R J,et al.Ductile fracture initiation,propagation and arrest in cylindrical vessels[M]//Fracture Toughness.ASTM STP 514,1972:70-81.
  • 5ANSI/ASME B31G-1991,Manual for determining the remaining strength of corroded pipelines[S].
  • 6CAN/CSA-Z184-M86-1986,Gas pipeline systems[S].
  • 7DNV RP F101-1999,Corroded Pipelines[S].
  • 8API RP 579-2000,Recommended practice for fitness-for-service[S].
  • 9Ingmarsson Karl.Fitness-for-service and decisions for petroleum and chemical equipment[M] // Pvp vol 315.New York:ASME,1995:1-6.
  • 10Zheng M,Zheng X.Expressions for predicting the elasticity modulus of materials reinforced by second phase grains[J].Metallurgical Transaction,1991,22A(8):507-511.

共引文献100

同被引文献89

引证文献6

二级引证文献76

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部