Corrosion Failure Reason and Protection Measure of Oil well Production String in Bohai L Oilfield
Received:May 18, 2020  Revised:October 10, 2020
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DOI:10.7643/issn.1672-9242.2021.01.011
KeyWord:oil well  production string  corrosion  dissolved oxygen  chloridion  sulfate reducing bacteria  erosion
              
AuthorInstitution
CHEN Hua-xing CNOOC China CO., Ltd., Tianjin Branch, Tianjin , China
PANG Ming CNOOC China CO., Ltd., Tianjin Branch, Tianjin , China
ZHAO Shun-chao CNOOC China CO., Ltd., Tianjin Branch, Tianjin , China
WANG Yu-fei CNOOC China CO., Ltd., Tianjin Branch, Tianjin , China
FANG Tao CNOOC China CO., Ltd., Tianjin Branch, Tianjin , China
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Abstract:
      The frequent corrosion failure and perforation of some oil well production strings in Bohai L Oilfield has a strong impact on normal production of oilfield. In order to prolong attended time of downhole pipe string, this paper analyzes the corrosion failure reason and protection measure of downhole pipe string. The failed pipe strings and corrosion product are studied by macroscopic morphology observing, metallographic structure analyzing and scanning electron microscope. Meanwhile corrosion reason is analyzed from ion composition of oilfield water, corrosion gas, bacteria and erosion. The result indicates that oil well production string of L oilfield has partial perforation and breakage. The inner surface of production string appears ulcerous corrosion and its colour is tawny and black. Metallographic structure of the failure pipe strings is composed of pearlite and ferrite, which is similar to matrix, and shows faveolate characteristic caused by corrosion. The main corrosion products are Fe, O and C. In conclusion, the key reason for the corrosion of oil well string in L Oilfield is that the dissolved oxygen in oilfield water exceeds the standard by 9 times, the chloridion concentration is greater than 3,500 mg/L, and sulfate reducing bacteria exceed the standard by 4 times, aggravating the partial corrosion of production string. Moreover, the flow state of the fluid at the intake of the electric submersible pump separator is changed to rotational flow, and the flow rate is greatly increased, resulting in erosion and aggravating the corrosion failure of the separator. It is suggested that L Oilfield should strengthen the monitoring and control of dissolved oxygen and chloridion in oilfield water. The corroded oil well should adopt anti-corrosion pipe and pump. In addition, the erosion resistance of separator should be improved.
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