Corrosion behavior of steels for CO2 injection

被引:84
作者
Yevtushenko, O. [1 ]
Bettge, Fl [1 ]
Bohraus, S. [1 ]
Baesslera, R. [1 ]
Pfennig, A. [2 ]
Kranzmann, A. [1 ]
机构
[1] Fed Inst Mat Res & Testing, Berlin, Germany
[2] Univ Appl Sci, Berlin, Germany
关键词
CCS; Injection tubing; Corrosion; Safety; Carbon steel; High alloy steel; Saline fluid; Supercritical CO2; CARBON-DIOXIDE; HEAT-TREATMENT; PITTING CORROSION; CAPTURE; CCS; TRANSPORT; IMPLEMENTATION; RESISTANCE; PRESSURE; FLOW;
D O I
10.1016/j.psep.2013.07.002
中图分类号
X [环境科学、安全科学];
学科分类号
083001 [环境科学];
摘要
The process chain for Carbon Capture and Sequestration (CCS) includes tubing for injection of CO2 into saline aquifers. The compressed CO2 is likely to contain specific impurities; small concentrations of SO2 and NO2 in combination with oxygen and humidity are most harmful. In addition, CO2 saturated brine is supposed to rise in the well when the injection process is interrupted. The material selection has to ensure that neither CO2 nor brine or a combination of both will leak out of the inner tubing. In this comprehensive paper the investigated materials range from low-alloy steels and 13% Cr steels up to high-alloy materials. Electrochemical tests as well as long term exposure tests were performed in CO2, in brine and combination of both; pressure was up to 100 bar, temperature up to 60 degrees C. Whereas the CO2 stream itself can be handled using low alloy steels, combinations of CO2 and brine require more resistant materials to control the strong tendency to pitting corrosion. The corrosion behavior of heat-treated steels depends on factors such as microstructure and carbon content. For different sections of the injection tube, appropriate materials should be used to guarantee safety and consider cost effectiveness. (C) 2013 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:108 / 118
页数:11
相关论文
共 44 条
[1]
Anwar S., 2011, CARBONDIOXIDE THERMO
[2]
CO2 Capture in the Cement Industry [J].
Barker, D. J. ;
Turner, S. A. ;
Napier-Moore, P. A. ;
Clark, M. ;
Davison, J. E. .
GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01) :87-94
[3]
Bassler R., 2012, PHYSIOCHEM MECH MAT, V9, P393
[4]
The structure, morphology and electrochemical impedance study of the passivation layers on the surface of the Co-Fe-Si-B-M amorphous metallic alloys [J].
Bednarska, L. ;
Kotur, B. ;
Kovbuz, M. ;
Budniok, A. ;
Lagiewka, E. .
XIII INTERNATIONAL SEMINAR ON PHYSICS AND CHEMISTRY OF SOLIDS, 2007, 79
[5]
Carter L.D., 2010, CAPTURE STORAGE CO2
[6]
Austenitizing treatment influence on the electrochemical corrosion behavior of 0.3C-14Cr-3Mo martensitic stainless steel [J].
Choi, Yoon-Seok ;
Kim, Jung-Gu ;
Park, Yong-Soo ;
Park, Jee-Yong .
MATERIALS LETTERS, 2007, 61 (01) :244-247
[7]
Corrosion of pipelines used for CO2 transport in CCS: Is it a real problem? [J].
Cole, Ivan S. ;
Corrigan, Penny ;
Sim, Samson ;
Birbilis, Nick .
INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2011, 5 (04) :749-756
[8]
Microstructure and pitting corrosion resistance of annealed duplex stainless steel [J].
Cvijovic, Z. ;
Radenkovic, G. .
CORROSION SCIENCE, 2006, 48 (12) :3887-3906
[9]
Davis J.R., 2000, Corrosion: Understanding the Basics
[10]
Dugstad A., 2013, CORROSION 2013