Research progress on CO2 corrosion mechanism and prediction model of natural gas pipelines

被引：0

作者：

Xie F. ^{[1
,2
]}

Li J. ^{[1
,2
]}

Wang X. ^{[3
]}

Ma C. ^{[4
]}

Su Y. ^{[1
,2
]}

Sun X. ^{[1
,2
]}

机构：

[1] College of Petroleum and Natural Gas Engineering, Liaoning Petrochemical University, Fushun

[2] Liaoning Key Laboratory of Oil & Gas Storage and Transportation Technology, Fushun

[3] PipeChina Eastern Crude Oil Storage and Transportation Co., Xuzhou

[4] Offshore Oil Engineering Co., Ltd., Tianjin

来源：

Natural Gas Industry | 2021年 / 41卷 / 10期

关键词：

CO[!sub]2[!/sub] corrosion; Corrosion mechanism; Corrosion product film; Corrosion rate prediction; Empirical model; Mechanistic model; Natural gas pipeline; Semi-empirical model;

D O I：

10.3787/j.issn.1000-0976.2021.10.012

中图分类号：

学科分类号：

摘要：

The CO2 corrosion mechanism from three aspects of homogeneous chemical reaction, electrochemical reaction, and mass transfer process was investigated along with the key factors influencing CO2 corrosion. The latest progress of the corresponding CO2 corrosion rate prediction model is discussed. Based on the latest understanding on CO2 corrosion mechanism, various models were compared in terms of mechanism and expandability. The current research studied on CO2 corrosion mechanism are mainly based on an ideal solution environment system, and in the future, it is necessary to study the CO2 corrosion mechanism of a non-ideal solution system. The reaction mechanism of CO2 corrosion has not been figured out, and whether CO2 could directly participate in the anodic reaction and H2CO3 can be directly reduced is still controversial, which needs further studying. The current corrosion rate prediction model only considers electrochemical corrosion factors, but does not consider the influence of complex flow in pipelines, so it is necessary to establish a prediction model which can reflect the actual working conditions of pipelines more accurately.

引用

页码：109 / 118

页数：9

共 60 条

[1] LI Yuan, LIU Shichang, ZHANG Yinhui, Study on analysis method of internal corrosion affecting factor under the coexistence of CO2 and H2S in surface gathering system, Chemical Engineering of Oil & Gas, 49, 1, pp. 82-86, (2020)
[2] CHENG Yuanpeng, BAI Yu, ZHENG Dukui, Et al., Test on the corrosion behavior of X65 steel in the simulated CO2/oil/water environment, Oil & Gas Storage and Transportation, 38, 8, pp. 863-869, (2019)
[3] ZHANG Lei, Influence of temperature on 5 typical steel corrosion behavior under supercritical CO2 condition, Oil & Gas Storage and Transportation, 39, 9, pp. 1031-1036, (2020)
[4] NESIC S, SUN W., 2.25-corrosion in acid gas solutions, Shreir's Corrosion, pp. 1270-1298, (2010)
[5] KAHYARIAN A, SINGER M, NESIC S., Modeling of uniform CO2 corrosion of mild steel in gas transportation systems: A review, Journal of Natural Gas Science and Engineering, 29, pp. 530-549, (2016)
[6] DE WAARD C, MILLIAMS D E., Carbonic acid corrosion of steel, Corrosion, 31, 5, pp. 177-181, (1975)
[7] KAHYARIAN A, NESIC S., A new narrative for CO2 corrosion of mild steel, Journal of the Electrochemical Society, 166, 11, pp. 3048-3063, (2019)
[8] KAHYARIAN A, ACHOUR M, NESIC S., 34-mathematical modeling of uniform CO2 corrosion, Trends in Oil and Gas Corrosion Research and Technologies, pp. 805-849, (2017)
[9] NESIC S, POSTLETHWAITE J, OLSEN S., An electrochemical model for prediction of corrosion of mild steel in aqueous carbon dioxide solutions, Corrosion, 52, 4, pp. 280-294, (1996)
[10] NESIC S., Key issues related to modelling of internal corrosion of oil and gas pipelines--a review, Corrosion Science, 49, 12, pp. 4308-4338, (2007)

← 1 2 3 4 5 6 →