Citation: | GUO Shao-qiang, ZHU Hai-shan, LIU Xin, LU Min-xu, XU Li-ning, QIN Hui-min. Prediction Model of Top-of-the-line CO2 Corrosion in Gas Pipeline[J]. Corrosion & Protection, 2014, 35(5): 469-472. |
[1] |
DE Waard C, LOTZ U,DUGSTA A. Influence of liquid flow velocity on CO2 corrosion:a semi-empirical model[C]//50th NACE Annual Conf.Houston TX:NACE International,1995:95128.
|
[2] |
DUGSTAD A,NYBORG R,SEIERSTEN M. Flow assurance of pH stabilized wet gas pipelines[C]//58th NACE Annual Conf.Houston TX:NACE International,2003:03314.
|
[3] |
ZHANG Z,HINKSON D,SINGER M,et al. A mechanistic model of top-of-the-line corrosion[J]. Corrosion,2007,63(11):1051.
|
[4] |
NORDSVEEN M,NESIC S,NYBORG R,et al. A mechanistic model for carbon dioxide corrosion of mild steel in the presence of protective iron carbonate films-Part 1:theory and verification[J]. Corrosion,2002,59(5):443.
|
[5] |
SUN W,NESIC S. Kinetics of corrosion layer formation:Part 1-iron carbonate layers in carbon dioxide corrosion[J]. Corrosion,2008,64(4):334.
|
[6] |
QIN H,XU L,CHANG W,et al. Top of the line corrosion under low temperature and high condensation rate conditions[C]//64th NACE Annual Conf.Houston TX:NACE International,2011:11328.
|