Study on the Flow- Induced Corrosion of P110 Oil Tube with an Electrochemical Method

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P110 Steel Flow-induced corrosion Electrochemical Method Abstract. Electrochemical measurements have been used to investigate the flow-induced corrosion behaviors of P110 oil tube in 3.5wt% NaCl solution. The corrosion rates were calculated by linear polarization resistance method and weak polarization method respectively. The results demonstrated that corrosion rate of P110 steel increases sharply with the flow velocity increase when the impact angle is 30°, but it reach the first plateau when the fluid velocity changes from 5.6 m/s to 7.8 m/s and the corrosion rate increases sharply again when the velocity beyond 7.8 m/s. After that, corrosion rate decrease when the velocity is more than 10.0m/s. It is demonstrated that the corrosion rate of steel P110 is controlled by cathode reaction of oxygen diffusion in the 3.5 wt % NaCl solution when the flow velocity is over 10.0m/s.

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396-399

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April 2013

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] YiHua Dou, AiRong Xu, FuXiang Zhang etc, The Review of High temperature high pressure well testing for oil well completion problems, Journal of Petroleum Machinery,4 (2008) 140-142.

Google Scholar

[2] Achebo, Joseph I. Quantitative Determination of Fluid Flow Induced Corrosion Rate of an Oil Pipeline, International Conference on Engineering Computation, 2(2009) 250-252.

DOI: 10.1109/icec.2009.58

Google Scholar

[3] Zhang Yugui, Yao Zhiming, Zhang Yusheng etc, Erosion corrosion synergism and erosion corrosion resistant alloy development, Acta Metal Sin, 4 (2000) 51-54.

Google Scholar

[4] Stack M M, Abd EI-Badia T M ,Some comments on mapping the combined effects of slurry concentration, impact velocity and electrochemical potential on the erosion-corrosion of WC/Co - Cr coatings.Wear, 264 (2008) 826-837.

DOI: 10.1016/j.wear.2007.02.025

Google Scholar

[5] Zhang Zhi, The corrosion mechanism of oil well pipe and protective coating research on the severe environment, Southwest petroleum university,( 2005).

Google Scholar

[6] Chunan Cao, The theory of corrosive electrochemistry, third ed, Chemical Industry Press (CIP), Beijing, (2004).

Google Scholar

[7] Xu zhe, Research on the erosion-corrosion behavior of P110 steel in liquid-solid two phase flow, Northeast Petroleum University, (2011).

Google Scholar

[8] GuoXian Zhao, Xianghong Lu, Effect of Flow Rate on CO2 Corrosion Behavior, Materials engineering, 8 (2008) 5-8.

Google Scholar

[9] Tait WS, An introduction to electrochemical corrosion testing for practicing engineers and scientists, Pair ODocs Publications, (1994).

Google Scholar

[10] XingLing Tian,YuZhen Lin,JingJun Liu,et al,Carbon steel in liquid/solid two phase tube flow wear corrosion electrochemical behavior,China journal of corrosion and protection, 1(2004)50-53.

Google Scholar

[11] Xianghong Lu, yanqing Yang, guoxian Zhao etc, N80 steel of high temperature high pressure CO2 corrosion electrochemical characteristics. Journal of materials science and engineering, 23 (2004) 697-700.

Google Scholar

[12] Yong Xing-yue, Lin Yu-zhen, Liu Jing-jun etc, Flow-induced corrosion kinetics model of carbon steel in flow loop system, Journal of Chemical Industry and Engineering ( China), 53 (2002) 680-684.

Google Scholar