High pressure and high temperature corrosion performance of high strength 15Cr martensitic stainless steel was studied in different severe environments—live acid (10%HCl+1.5%HF+3%HAc+5.1% corrosion inhibitor), spent acid and formation water containing CO2. The results show that the corrosion of high strength 15Cr martensitic stainless steel in live acid is most serious, and the uniform corrosion rate is far greater than those in spent acid and formation water containing CO2 corrosion environments, but all of them can be acceptable for oilfield. Acidizing corrosion inhibitor displays a good matching ability with the high strength 15Cr martensitic stainless steel in terms of decreasing the uniform corrosion rate, which changes mainly the anodic process of high strength 15Cr martensitic stainless steel. The corrosion potential moves to the positive direction, thus the corrosion current density decreases significantly. There are some different degrees of pitting of high strength 15Cr martensitic stainless steel after corrosion tests in live acid, spent acid and formation water containing CO2, and the pitting density aggravates significantly and the maximum pit depth decreases in the corrosion sequence.
Abstract
High pressure and high temperature corrosion performance of high strength 15Cr martensitic stainless steel was studied in different severe environments—live acid (10%HCl+1.5%HF+3%HAc+5.1% corrosion inhibitor), spent acid and formation water containing CO2. The results show that the corrosion of high strength 15Cr martensitic stainless steel in live acid is most serious, and the uniform corrosion rate is far greater than those in spent acid and formation water containing CO2 corrosion environments, but all of them can be acceptable for oilfield. Acidizing corrosion inhibitor displays a good matching ability with the high strength 15Cr martensitic stainless steel in terms of decreasing the uniform corrosion rate, which changes mainly the anodic process of high strength 15Cr martensitic stainless steel. The corrosion potential moves to the positive direction, thus the corrosion current density decreases significantly. There are some different degrees of pitting of high strength 15Cr martensitic stainless steel after corrosion tests in live acid, spent acid and formation water containing CO2, and the pitting density aggravates significantly and the maximum pit depth decreases in the corrosion sequence.
关键词
high strength 15Cr martensitic stainless steel /
live acid /
spent acid /
CO2 corrosion
{{custom_keyword}} /
Key words
high strength 15Cr martensitic stainless steel /
live acid /
spent acid /
CO2 corrosion
{{custom_keyword}} /
{{custom_sec.title}}
{{custom_sec.title}}
{{custom_sec.content}}
参考文献
[1] Boles J, Ke M J, Parker C. Corrosion Inhibition of New 15 Chromium Tubulars in Acid Stimulation Fluids at High Temperatures[C]. The 2009 SPE Annual Technical Conference and Exhibition held in New Orleans, Louisiana, USA, 4-7 October, 2009.
[2] Wang L C, Li M L, Cheng W Q, etc. Application of Acidification Fracturing Method in Carbonate Thermal Reservoir [J]. Hydrogeology and Engineering Geology, 2010,37(5): 128-132.
[3] SY/T 5405-1996, Test Methods & Evaluation of Acidizing Corrosion Inhibitor Performance[S].
[4] NACE RP 0775-2005, Preparation, Installation, Analysis, and Interpretation of Corrosion Coupons in Oilfield Operations[S].
[5] Kimura M, Sakata K. Corrosion resistance of martensitic stainless OCTG in severe corrosion environments[C]. 62th NACE Annual Conference, Nashville, Tennessee, March 11-15, 2007. Houston: Omnipress, 2007.
[6] Boles J, Ke M J, Parker C. Corrosion Inhibition of New 15 Chromium Tubulars in Acid Stimulation Fluids at High Temperatures[C]. The 2009 SPE Annual Technical Conference and Exhibition held in New Orleans, Louisiana, USA, 4-7 October, 2009.
[7] Bayol E, Gürten T, Ali G A, et al.Interactions of some Schiff base compounds with mild steel surface in hydrochloric acid solution[J].Materials Chemistry and Physics,2008, 112(2):624-630.
[8] Ke M J, Boles J. Corrosion Behavior of Various 13 Chromium Tubulars in Acid Stimulation Fluids[C]. The 1st International Symposium on Oilfield Corrosion held in Aberdeen, Scotland, U.K., 28 May, 2004.
[9] Nasr-El-Din H A, Khuraidah A, Kritzler T, et al. Recent Developments in High-Temperature Acidizing with Super 13Cr Completions Laboratory Testing[C]. The 2002 SPE Annual Technical Conference and Exhibition held in New Orleans, Louisiana, USA, 4-7 October, 2002.
[10] Trasatti S, Scoppio L. H2S and CO2 corrosion of some 9Cr-1Mo alloys for downhole application. 56th NACE Annual Conference, Houston, Texas, March 11-16, 2001[C]. Houston: Omnipress, 2001.
{{custom_fnGroup.title_cn}}
脚注
{{custom_fn.content}}
基金
Program for New Century Excellent Talents In University
{{custom_fund}}