The corrosion behavior in CO2 medium of 20# steel under the (CO2/aqueous solution) gas-liquid two-phase stratified flow condition

被引:1
作者
Yang Gui-rong [1 ]
Song Wen-ming [2 ]
Wang Fu-qiang [1 ]
Ma Ying [1 ]
Hao Yuan [1 ]
机构
[1] Lanzhou Univ Technol, State Key Lab Adv Proc & Recycling Nonferrous Met, Lanzhou 730050, Peoples R China
[2] Lanpec Technol Ltd, Lanzhou 730070, Peoples R China
基金
中国国家自然科学基金;
关键词
20# seamless steel; CO2; corrosion; stratified flow; corrosion products characteristics; mechanism; CARBON-DIOXIDE; INHIBITOR PERFORMANCE; PIPELINE STEEL; MILD-STEEL; OIL; PREDICTION; IMIDAZOLINE; ISSUES; MODEL;
D O I
10.1088/2053-1591/aae667
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
The corrosion rate, morphology, and composition of corrosion products of 20# seamless steel in CO2 medium under gas-liquid two-phase stratified flow conditions (CO2/aqueous solution) have been investigated using the weight loss method, scanning electron microscopy with energy-dispersive x-ray spectroscopy, and x-ray diffraction. The forming mechanism of corrosion products has been discussed. Results showed the irregular zigzag trend of the corrosion rate curve with the gradual extension of corrosion time. The corrosion rate peaked at corrosion times of 4 and 8 h, with the values reaching 1.49 and 0.647 mm/a, respectively. At the beginning of the corrosion process, a layer of special iron oxide formed rapidly on the 20# steel surface. The local corrosion products with cell shape precipitate and grow on the special iron oxide surface with the extension of corrosion time, and the initial corrosion product is mainly strip-shaped along the CO2 gas flow direction. The local cellular corrosion products extended along the perpendicular direction of gas flow to gradually form an entire covering product layer with the extension of corrosion time. The main phases of corrosion products include FeCO3 and iron oxides. The loose inner layer mainly comprised Fe3C and little amount FeCO3, whereas the dense outer layer was mainly composed of FeCO3 and a few iron oxides. The loose corrosion product layer presented a period of densification after formation.
引用
收藏
页数:10
相关论文
共 27 条
[11]  
Kongshaug KO, 2004, CORROSION
[12]   Corrosion of pipelines in CO2-saturated oil-water emulsion flow studied by electrochemical measurements and computational fluid dynamics modeling [J].
Li, Qiang ;
Hu, Haitao ;
Cheng, Y. Frank .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2016, 147 :408-415
[13]  
Li W., 2015, P CORROSION 2015, pNACE
[14]   Use of Carbon Steel for Construction of Post-combustion CO2 Capture Facilities: A Pilot-Scale Corrosion Study [J].
Li, Wei ;
Landon, James ;
Irvin, Bradley ;
Zheng, Liangfu ;
Ruh, Keith ;
Kong, Liang ;
Pelgen, Jonathan ;
Link, David ;
Figueroa, Jose D. ;
Thompson, Jesse ;
Nikolic, Heather ;
Liu, Kunlei .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2017, 56 (16) :4792-4803
[15]   Investigation of Pseudo-Passivation of Mild Steel in CO2 Corrosion [J].
Li, Wei ;
Brown, Bruce ;
Young, David ;
Nesic, Srdjan .
CORROSION, 2014, 70 (03) :294-302
[16]   Water Reactivity in the Liquid and Supercritical CO2 Phase: Has Half the Story Been Neglected? [J].
McGrail, B. P. ;
Schaef, H. T. ;
Glezakou, V. -A. ;
Dang, L. X. ;
Owen, A. T. .
GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01) :3415-3419
[17]   A time-variant corrosion wastage model for subsea gas pipelines [J].
Mohd, Mohd Hairil ;
Kim, Do Kyun ;
Kim, Dong Woo ;
Paik, Jeom Kee .
SHIPS AND OFFSHORE STRUCTURES, 2014, 9 (02) :161-176
[18]   Effects of Multiphase Flow on Internal CO2 Corrosion of Mild Steel Pipelines [J].
Nesic, S. .
ENERGY & FUELS, 2012, 26 (07) :4098-4111
[19]   Key issues related to modelling of internal corrosion of oil and gas pipelines - A review [J].
Nesic, Srdjan .
CORROSION SCIENCE, 2007, 49 (12) :4308-4338
[20]   Co2 corrosion inhibition of X-120 pipeline steel by a modified imidazoline under flow conditions [J].
Ortega-Toledo, D. M. ;
Gonzalez-Rodriguez, J. G. ;
Casales, M. ;
Martinez, L. ;
Martinez-Villafane, A. .
CORROSION SCIENCE, 2011, 53 (11) :3780-3787