Effects of CO2 gassy-supercritical phase transition on corrosion behaviors of carbon steels in saturated vapor environment

De-zhi Zeng , Zhi-yao Huang , Zhi-ming Yu , Shan-zhi Shi , Yong-gang Yi , Cong-ping Liu , Gang Tian , Yi-cheng Sun

Journal of Central South University ›› 2021, Vol. 28 ›› Issue (2) : 325 -337.

PDF
Journal of Central South University ›› 2021, Vol. 28 ›› Issue (2) : 325 -337. DOI: 10.1007/s11771-021-4605-1
Article

Effects of CO2 gassy-supercritical phase transition on corrosion behaviors of carbon steels in saturated vapor environment

Author information +
History +
PDF

Abstract

Corrosion behaviors of P110 and N80 tubular steels in CO2 gas phase and supercritical (S-CO2) phase in a saturated water vapor environment were explored in corrosion weight loss experiments by SEM, EDS, XRD, XPS and cross-section analysis techniques. With the increase in CO2 partial pressure, the average corrosion rate increased first and then decreased. The average corrosion rate reached the maximum value under the near-critical pressure. When CO2 partial pressure further increased to be above the critical pressure, the average corrosion rate gradually decreased and local aggregation of molecules was weakened.

Keywords

carbon capture and storage / supercritical carbon dioxide / corrosion product / corrosion mechanism

Cite this article

Download citation ▾
De-zhi Zeng, Zhi-yao Huang, Zhi-ming Yu, Shan-zhi Shi, Yong-gang Yi, Cong-ping Liu, Gang Tian, Yi-cheng Sun. Effects of CO2 gassy-supercritical phase transition on corrosion behaviors of carbon steels in saturated vapor environment. Journal of Central South University, 2021, 28(2): 325-337 DOI:10.1007/s11771-021-4605-1

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

GaleJ, DavisonJ. Transmission of CO2-safety and economic considerations [J]. Energy, 2003, 29(9): 1319-1328

[2]

ZhangG A, LiuD, LiY Z, GuoX P. Corrosion behaviour of N80 carbon steel in formation water under dynamic supercritical CO2 condition [J]. Corrosion Science, 2017, 120: 107-120

[3]

NesicS, PostlethwaiteJ. Modelling of CO2 corrosion mechanisms [M]. Modelling Aqueous Corrosion, 1994, Dordrecht, Springer, 317335

[4]

LiuZ-y, ZhaoT-l, LiuR-k, JiaJ-h, DuC-w, LiX-G. Influence factors on stress corrosion cracking of P110 tubing steel under CO2 injection well annulus environment [J]. Journal of Central South University, 2016, 23(4): 757-764

[5]

XuM-h, LiW-h, ZhouY, YangX-x, WangZ, LiZ. Effect of pressure on corrosion behavior of X60, X65, X70, and X80 carbon steels in water-unsaturated supercritical CO2 environments [J]. International Journal of Greenhouse Gas Control, 2016, 51: 357-368

[6]

XiangY, LiC, HesitaoW, LongZ-w, YanW. Understanding the pitting corrosion mechanism of pipeline steel in an impure supercritical CO2 environment [J]. Journal of Supercritical Fluids, 2018, 138: 132-142

[7]

SuiP-f, SunJ-b, HuaY, LiuH-f, ZhouM-n, ZhangY-c, LiuJ-h, WangY. Effect of temperature and pressure on corrosion behavior of X65 carbon steel in water-saturated CO2 transport environments mixed with H2S [J]. International Journal of Greenhouse Gas Control, 2018, 73: 60-69

[8]

HuaY, BarkerR, NevilleA. Comparison of corrosion behaviour for X-65 carbon steel in supercritical CO2-saturated water and water-saturated/unsaturated supercritical CO2 [J]. Journal of Supercritical Fluids, 2015, 97: 224-237

[9]

SunC, SunJ-b, LiuS-b, WangY. Effect of water content on the corrosion behavior of X65 pipeline steel in supercritical CO2-H2O-O2-H2S-SO2 environment as relevant to CCS application [J]. Corrosion Science, 2018, 137: 151-162

[10]

SunC, WangY, SunJ-b, LinX-q, LiX-d, LiuH-f, ChengX-K. Effect of impurity on the corrosion behavior of X65 steel in water-saturated supercritical CO2 system [J]. Journal of Supercritical Fluids, 2016, 116: 70-82

[11]

SunC, SunJ-b, WangY, SuiP-f, LinX-q, LiuH-f, ChengX-k, ZhouM-N. Effect of impurity interaction on the corrosion film characteristics and corrosion morphology evolution of X65 steel in water-saturated supercritical CO2 system [J]. International Journal of Greenhouse Gas Control, 2017, 65: 117-127

[12]

SunJ-b, SunC, WangY. Effects of O2 and SO2 on water chemistry characteristics and corrosion behavior of X70 pipeline steel in supercritical CO2 transport system [J]. Industrial & Engineering Chemistry Research, 2018, 57(6): 2365-2375

[13]

SunJ-b, SunC, ZhangG-a, LiX-d, ZhaoW-m, JiangT, LiuH-f, ChengX-k, WangY. Effect of O2 and H2S impurities on the corrosion behavior of X65 steel in water-saturated supercritical CO2 system [J]. Corrosion Science, 2016, 107: 31-40

[14]

ChoiY S, NešićS. Effect of water content on the corrosion behavior of carbon steel in supercritical CO2 phase with impurities [C]. Corrosion 2011, 2011, Houston, Texas, NACE International, 11377

[15]

HuaY, BarkerR, CharpentierT, WardM, NevilleA. Relating iron carbonate morphology to corrosion characteristics for water-saturated supercritical CO2 systems [J]. The Journal of Supercritical Fluids, 2015, 98: 183-193

[16]

GuoS-p, XuL-n, ZhangL, ChangW, LuM-X. Characterization of corrosion scale formed on 3Cr steel in CO2-saturated formation water [J]. Corrosion Science, 2016, 110: 123-133

[17]

BeckJ, FedkinaM, LvovS, Ziomek-MorozM E, HolcombG, TylczakJ, AlmanD. In situ electrochemical corrosion measurements of carbon steel in supercritical CO2 using a membrane-coated electrochemical probe [J]. ECS Transactions, 2013, 45(19): 39-50

[18]

ThodlaR, FrancoisA, SridharN. Materials performance in supercritical CO2 environments [C]. Corrosion 2009, 2009, Atlanta, Georgia, NACE International, 09255

[19]

SimS, BocherF, ColeI S, ChenX B, BirbilisN. Investigating the effect of water content in supercritical CO2 as relevant to the corrosion of carbon capture and storage pipelines [J]. Corrosion, 2014, 70(2): 185-195

[20]

BeckJ, LvovS, FedkinM V, Ziomek-MorozM, HolcombG, TylczakJ, AlmanD. Electrochemical system to study corrosion of metals in supercritical CO2 fluids [C]. Corrosion 2011, 2011, Houston, Texas, NACE International, 11380

[21]

TuckerS C, MaddoxM W. The effect of solvent density inhomogeneities on solute dynamics in supercritical fluids: a theoretical perspective [J]. The Journal of Physical Chemistry B, 1998, 102: 2437-2453

[22]

NishikawaK, OchiaiH, SaitowK, MoritaT. Static inhomogeneity of supercritical ethylene studied by small-angle X-ray scattering [J]. Chemical Physics, 2003, 286(23): 421-430

[23]

TachikawaT, AkiyamaK, YokoyamaC, Tero-KubotaS. Local density effects on the hyperfine splitting constant and line width of TEMPO radical in gaseous and supercritical carbon dioxide [J]. Chemical Physics Letters, 2003, 376(34): 350-357

[24]

EgorovS A. Local density enhancement in neat supercritical fluids: Dependence on the interaction potential [J]. Chemical Physics Letters, 2002, 354(12): 140-147

[25]

MukhopadhyayM, DalviS V. Partial molar volume fraction of solvent in binary (CO2-solvent) solution for solid solubility predictions [J]. The Journal of Supercritical Fluids, 2004, 29(3): 221-230

[26]

ZhangJ-l, LiuJ-c, GaoL, ZhangX-g, HouZ-s, HanB-x, WangJ, DongB-z, RongL-x, ZhaoH. Small-angle X-ray scattering study on correlation length and density fluctuations in a supercritical CO2-water mixture [J]. Fluid Phase Equilibria, 2002, 198(2): 251-256

[27]

ZhangJ-l, ZhangX-g, HanB-x, HeJ, LiuZ-m, YangG-Y. Study on intermolecular interactions in supercritical fluids by partial molar volume and isothermal compressibility [J]. The Journal of Supercritical Fluids, 2002, 22(1): 15-19

[28]

HessG, FroitzheimH, BaumgartnerC. The adsorption and catalytic decomposition of CO2 on Fe (111) surfaces studied with high resolution EELS [J]. Surface Science, 1995, 331: 138-143

[29]

FernandesF W, CamposT M B, CividanesL S, SimonettiE A N, ThimG P. Adsorbed water on iron surface by molecular dynamics [J]. Applied Surface Science, 2016, 362: 70-78

[30]

BaiR-s, YangR T. A thermodynamically consistent Langmuir model for mixed gas adsorption [J]. Journal of Colloid and Interface Science, 2001, 239(2): 296-302

[31]

KravanjaG, ŠkergetM, KnezŽ, HrnčičM K. Diffusion coefficients of water and propylene glycol in supercritical CO2 from pendant drop tensiometry [J]. The Journal of Supercritical Fluids, 2018, 133: 1-8

[32]

TAYLOR R, KRISHNA R. Multicomponent mass transfer [M]. John Wiley & Sons, 1993.

[33]

MagalhaesA L, DaS F A, SilvaC M. Free-volume model for the diffusion coefficients of solutes at infinite dilution in supercritical CO2 and liquid H2O [J]. The Journal of Supercritical Fluids, 2013, 74: 89-104

[34]

Mora-MendozaJ L, TurgooseS. Fe3C influence on the corrosion rate of mild steel in aqueous CO2 systems under turbulent flow conditions [J]. Corrosion Science, 2002, 44(6): 1223-1246

[35]

PessuF, BarkerR, NevilleA. Understanding pitting corrosion behavior of X65 carbon steel in CO2-saturated environments: The temperature effect [J]. Corrosion, 2016, 72(1): 78-94

[36]

WuQ-l, ZhangZ-h, DongX-m, YangJ-Q. Corrosion behavior of low-alloy steel containing 1% chromium in CO2 environments [J]. Corrosion Science, 2013, 75: 400-408

[37]

HouS X, MaitlandG C, TruslerJ P M. Measurement and modeling of the phase behavior of the (carbon dioxide+ water) mixture at temperatures from 298.15 K to 448.15 K [J]. The Journal of Supercritical Fluids, 2013, 73: 87-96

AI Summary AI Mindmap
PDF

111

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/