Pengli Ge1,2, Wenbin Pang1,2, Zhiming Liu1,2, Lili He1,2, and Jiang Meng3This email address is being protected from spambots. You need JavaScript enabled to view it.
1Northwest Company of China Petroleum and Chemical Corporation, SINOPEC, Urumqi, 830011, China
2Key Laboratory of Enhanced Recovery for Fracture-cave Oil Reservoir, SINOPEC, Urumqi, 830011, China
3School of Petroleum Engineering, Chongqing University of Science and Technology, Chongqing, 401331, China
Received: October 23, 2023 Accepted: April 14, 2024 Publication Date: June 9, 2024
Copyright The Author(s). This is an open access article distributed under the terms of the Creative Commons Attribution License (CC BY 4.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are cited.
In order to investigate the effect of typical ions in produced water in oil and gas fields on the pipeline corrosion behavior, the corrosion behavior of N20 steel by HCO−3 concentration in the environment with Cl−, Ca2+, Mg2+ and SO2−4 wasstudied bymeansof weight loss measurement and electrochemical tests. The effects of HCO−3 concentration on the corrosion of N20 steel were analyzed by means of optical microscope, scanning electron microscope, energy spectrum analyzer and electrochemical workstation. The results showed that in the range of HCO−3 concentration in this work, the water sample has an obvious trend of CaCO3 scaling. With the increase of HCO−3 concentration, the corrosion rate of N20 steel first increased and then decreased, and the corrosion control changed from discharge process and diffusion process to diffusion process. When the concentration of HCO−3 is 200 mg/L,theuniform corrosion rate reaches the maximum. Due to the different HCO−3 concentration, the density and distribution of the layers of scaling and corrosion products are different. Therefore, even if large-scale scaling occurs, local corrosion of N20 steel cannot be prevented due to the non-uniformity of scaling.
Keywords: produced water; HCO− 3 concentration; corrosion behavior; N20 steel
[1] S. Tang, Y. Li, W. Dai, and W. Hao, (2018) “Corrosion failure of 20# steel in the complicated environment" Oil Gas Storage and Transportation (In Chinese) 37(8): 909–915.
[2] X. Deng, K. Liao, F. Wang, S. Li, and D. Cai, (2018) “Study on the corrosion monitoring technology used in gas-gathering pipelines in high sour gas field" Chemical Engineering of Oil Gas (In Chinese) 47(3): 73–75.
[3] W. Fan, J. Gao, and C. Liu, (2018) “Effect of pitting corrosion depth on the performance of L360 pipeline under high acid conditions" Oil Gas Storage and Transporta tion (In Chinese) 37(2): 77–81.
[4] Y. Wu, S. Shi, J. Huang, H. Yu, D. Baojun, and D. Zeng, (2018) “Evaluation of corrosion resistance for low alloy steels in high temperature steam environment with CO2" Chemical Engineering of Oil Gas (In Chi nese) 46(4): 77–81.
[5] R. A. EI-Nagar, N. Khalil, Y. Atef, M. Nessim, and A. Ghanem,(2024) “Evaluation of ionic liquids based im idazolium salts as an environmentally friendly corrosion inhibitors for carbon steel in HCl solutions" Scientific Reports 14: 1889. DOI: 10.1038/s41598-024-52174-5.
[6] Y.-S. Choi, M. Colahan, and S. Neši´ c, (2023) “Effect of f low on the corrosion behavior of pipeline steel in super critical CO2 environments with impurities" Corrosion 79(5): 497–508. DOI: 10.5006/4199.
[7] Y.-S. Choi, S. Hassani, T. Nam Vu, S. Neši´c, A. Z. B. Abas, A. M. Nor, and M. F. Suhor, (2019) “Strategies for corrosion inhibition of carbon steel pipelines under supercritical CO2/H2S environments" Corrosion 75(10): 1156–1172. DOI: 10.5006/2765.
[8] Y.-S. Choi, S. Neši´ c, and H.-G. Jung, (2018) “Strategies for corrosion inhibition of carbon steel pipelines under supercritical CO2/H2S environments" Corrosion 74(5): 566–576. DOI: 10.5006/2705.
[9] T. Gu, D. Tang, Z. Wang, H. Chen, and H. Xie, (2019) “Effect of typical ions in the corrosion behavior of carbon steel in CO2 environment" Natural Gas Industry (In Chinese) 39(7): 106–112. DOI: none.
[10] C. Xiao, R. Cui, H. Yang, G. Su, and X. Yu, (2023) “Corrosion behavior of P110S carbon steel under high Cl high acid gas partial pressure" Corrosion Protection (In Chinese) 44(4): 21–28. DOI: none.
[11] Z. Wang, L. Zhang, X. Tang, Z. Zhang, and M. Lu, (2017) “The surface characterization and passive behavior of type 316L stainless steel in H2S containing conditions" Applied Surface Science 423(11): 457–464. DOI: 10.1016/j.apsusc.2017.06.214.
[12] X. Tang, L. Zhang, Z. Wang, J. Xue, and M. Lu, (2018) “Effect of SO42- on the passive and pitting behavior of 316L austenite stainless steel in a Cl- containing solution" Chinese Journal of Engineering (In Chinese) 40(3): 366–372. DOI: none.
[13] Y. Zhou, J. Zeng, and J. Zhang, (2008) “Effect of com ponent and temperature of the oil-well produced water on corrosion behavior of Q235 steel" Materials for Mechan ical Engineering (In Chinese) 32(12): 25–28. DOI: none.
[14] F.Long,W.Zheng,C.Chen,Z.Xu,andQ.Han,(2005) “Influence of temperature CO2 partial pressure, flow rate and pH value on uniform corrosion rate of X65 pipeline steel" Corrosion Protection (In Chinese) 07: 290–293. DOI: none.
[15] X. Yao and B. Wang, (2010) “The influence of electro magnetic field on interface between 45-steel and solution" Journal of Taiyuan University of Technology (In Chinese) 41(6): 692–695. DOI: none.
[16] Q. Deng, Y. Wang, W. He, and X. Wang, (2017) “Syn ergistic influence of anions and temperature on corrosion behavior of P110 steel in oilfield water" Materials Pro tection (In Chinese) 50(5): 12–17. DOI: none.
[17] S. Wang, (2015) “Effect of water content of crude oil on corrosion behavior of oil and gas tubular goods steel in supercritical CO2 system" Corrosion Science and Pro tection Technology (In Chinese) 27(1): 73–77. DOI: none.
[18] Q. Cai, S. Zhu, J. Li, Z. Feng, and L. Lv, (2016) “Cor rosion behavior of 20 steel in simulated working envi ronment of CO2 flooding" Corrosion Protection (In Chinese) 37(8): 653–656. DOI: none.
[19] G. Zhang, M. Lu, C. Chai, and Y. Wu, (2006) “Effect of HCO3- concentration on CO2 corrosion in oil and gas f ields" Journal of University of Science and Tech nology Beijing, Mineral, Metallurgy, Material 13(1): 44–49. DOI: 10.1016/S1005-8850(06)60012-1.
[20] T.E.Perez, (2013) “Corrosion in the oil and gas industry: an increasing challenge for materials" The Journal of the Minerals, Metals Materials Society 65(8): 1033 1042. DOI: 10.1007/s11837-013-0675-3.
[21] M. Desimone, G. Grundmerer, G. Gordillo, and S. Simison, (2011) “Amphiphilic amidoamine as an effective corrosion inhibitor for mild steel exposed to CO2 satu rated solution: polarization" Electrochimica Acta 56(8): 2990–2998. DOI: 10.1016/j.electacta.2011.01.009.
[22] C. Sun, Y. Wang, J. Sun, T. Jiang, W. Zhao, and Y. Zhang, (2015) “Investigation progress on corrosion be havior of supercritical CO2 transmission pipelines con taining impurities in CCS" Journal of Chinese Society for CorrosionandProtection(InChinese)35(5):379 385. DOI: none.
[23] Z. Zhu and M. Wang, (2014) “Theoretical deduction and experimental study on the reaction of bicarbonate with metal cation" Chinese Journal of Chemical Edu cation (In Chinese) 35(17): 64–67. DOI: none.
We use cookies on this website to personalize content to improve your user experience and analyze our traffic. By using this site you agree to its use of cookies.