西南石油大学学报(自然科学版) ›› 2016, Vol. 38 ›› Issue (6): 158-163.DOI: 10.11885/j.issn.1674-5086.2015.02.04.04

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Corrosion and Inhibition Performance Study of Oil Casing Steel in Calcium Chloride Solution

HUANG Qiuwei1, JIAN Lu2,3, LI Guoliang1, DU Zonghe4, WANG Xu2   

  1. 1. Formation Testing Company of Xibu Drilling Engineering Company, CNPC, Karamay, Xinjiang 834000, China;
    2. School of Material Science and Engineering, Southwest Petroleum University, Chengdu, Sichuan 610500, China;
    3. Deyang Carbonene Technology Co. Ltd., Deyang, Sichuan 618000, China;
    4. Xinjiang Oilfield Company, CNPC, Karamay, Xinjiang 834000, China
  • Received:2015-02-04 Online:2016-12-01 Published:2016-12-01

Abstract: In order to know the corrosion resistance of ordinary carbon steel in the regular killing fluid and find a way to control its corrosion condition, weight loss method and electrochemical methods were used to study N80 and P110 steel's corrosion situation and corrosion inhibition ability in 1.35 g/cm3 CaCl2 solution at standard pressure and different temperatures, high temperature and pressure, and different types of corrosion inhibitor, dosage. The experimental results showed that with increasing temperature the corrosion of N80 and P110 steel is intensified. And at the standard pressure with the temperature range of 60~80℃, the corrosion current density of the ordinary carbon steel raised from 10-6 A/cm2 to 10-5 A/cm2. At 4 MPa with temperature rising from 90℃ to 150℃, the corrosion rate increased an order of magnitude. At 80℃ with the amount of WLD31A 30 mg/L, it improved inhibition efficiency on N80 up to 95.51%, and that on P110 up to 93.11%. Within the range of 60~80℃, elevated temperatures help to improve WLD31A inhibition effect, the inhibition efficiency of N80 increases from 88.08% to 95.51% and P110 from 61.38% to 93.11%.

Key words: oil casing steel, calcium chloride solution, corrosion, inhibitor, well control fluid

CLC Number: