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Journal of Chinese Society for Corrosion and protection  2025, Vol. 45 Issue (6): 1639-1648    DOI: 10.11902/1005.4537.2025.053
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Corrosion Inhibition Performance of Triazine-derived Quaternary Ammonium Salts for Q235 Carbon Steel in High Temperature and High Pressure CO2 Containing 3.5%NaCl Solution
WU Chunsheng1, ZHANG Tianyong1, LI Bin1, YUAN Wenying1, ZHANG Xiaoou1, JIANG Shuang1,2(), WANG Huaiyuan1,2()
1 School of Chemical Engineering and Technology, Tianjin University, Tianjin 300354, China
2 Ningbo Key Laboratory of Green Petrochemical Carbon Emission Reduction Technology and Equipment, Ningbo 315000, China
Cite this article: 

WU Chunsheng, ZHANG Tianyong, LI Bin, YUAN Wenying, ZHANG Xiaoou, JIANG Shuang, WANG Huaiyuan. Corrosion Inhibition Performance of Triazine-derived Quaternary Ammonium Salts for Q235 Carbon Steel in High Temperature and High Pressure CO2 Containing 3.5%NaCl Solution. Journal of Chinese Society for Corrosion and protection, 2025, 45(6): 1639-1648.

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Abstract  

Amido-group triazine quaternary ammonium salt (CCDY) corrosion inhibitor was synthesized by nucleophilic substitution reaction and quaternary ammonium reaction with trichlorotriazine, dipropylamine and bromoacetamide as raw material. Then which was compounded with thiourea (TU) and sodium tungstate to acquire the complex inhibitor of optimal proportion, which was named CTLY. Next, the corrosion inhibition performance of the complex corrosion inhibitor CTLY for Q235 steel was assessed via static immersion test at 90 oC in 0.5 MPa CO2 containing 3.5%NaCl solution, accord with an orthogonal test arrangement, as well as electrochemical tests, surface morphology analysis and quantum chemical calculations. The results show that the corrosion inhibition rate of CTLY for Q235 steel can reach 96.64%. CTLY conforms to the Langmuir adsorption isothermal formula on the surface of Q235 steel, and the standard adsorption Gibbs free energy (ΔG0) is between -20 and -40 kJ/mol, correspondingly which is a mixed adsorption dominated by chemical adsorption. Electrochemical tests showed that CTLY was a mixed inhibitory corrosion inhibitor, while mainly inhibiting the anode reaction. The Nyquist plot shows a single-half arc, and the charge transfer impedance increases significantly with the increase of CTLY concentration. The surface morphology analysis further showed that CTLY had a good corrosion inhibition effect.

Key words:  triazine quaternary ammonium salt      high temperature and high pressure      orthogonal test method      CO2 corrosion inhibitor     
Received:  18 February 2025      32134.14.1005.4537.2025.053
ZTFLH:  TG174  
Fund: Ningbo Key Laboratory Open Fund(ZITJU2024-ZYDK037)
Corresponding Authors:  JIANG Shuang, E-mail: shuangjiang@tju.edu.cnWANG Huaiyuan, E-mail: wanghyjiji@163.com

URL: 

https://www.jcscp.org/EN/10.11902/1005.4537.2025.053     OR     https://www.jcscp.org/EN/Y2025/V45/I6/1639

Fig.1  Synthesis route of CCDY corrosion inhibitor
Fig.2  FTIR spectrum of CCDY
Fig.3  NMR spectra of CCDY: (a) 1H, (b) 13C
Fig.4  Corrosion inhibition rate of CCDY as a function of its concentration
Fig.5  Corrosion inhibition rates of CCDY inhibitors with different concentrations of TU (a) and Na2WO4 (b)
LevelABC
CCDYTUNa2WO4
12007525
222510050
325012575
Table 1  Main influencing factors of corrosion inhibition performance and their levels (mg·L-1)
No.ABCη / %
111192.53
221391.73
331290.40
412396.64
522292.79
632192.94
713290.40
823191.72
933392.66
K1279.57274.66277.19
K2276.24282.37273.59
K3276.00274.78281.03
k193.1991.5592.40
k292.0894.1291.20
k392.0091.5993.68
R1.192.572.48
Table 2  Results of L9 (34) orthogonal experiment
Fig.6  Potentiodynamic polarization curves of Q235 steel in 0.5 MPa CO2 saturated 3.5%NaCl solutions with the presences of CCDY and compound inhibitors at 80 oC
InhibitorEcorr / mVIcorr / μA·cm-2η / %
Blank-0.695150.4-
CCDY-0.67535.476.46
CTLY-0.66211.792.22
Table 3  Fitting results of potentiodynamic polarization curves in Fig.6
Fig.7  Nyquist (a), impedance module (b) and phase angle (c) plots of Q235 steel in 0.5 MPa CO2 saturated 3.5% NaCl solutions containing different concentrations of CTLY, and corresponding equivalent circuit model (d)
c / mg·L-1Rs / Ω·cm2Rct / Ω·cm2CPEdl / μF·cm-2χ2η / %
07.07468.2223.50.0026
2258.0481196.3145.60.001593.75
3006.7121445.1128.30.001294.82
3757.1982359.892.90.000596.82
4507.2561843.5104.60.000895.93
Table 4  Fitting parameters of EIS in Fig.7 for Q235 steel
Fig.8  Fitted lines of c/θ-c for CTLY
T / oCr2SlopeInterceptKL·mg-1ΔGkJ·mol-1
600.99940.98116.1330.0620-30.56
900.99920.98621.5550.0464-32.44
1200.99891.03614.3900.0695-36.44
Table 5  Linear regression parameters of c/θ-c and adsorption thermodynamic parameters for CTLY
Fig.9  Surface SEM micrographs of Q235 steel before (a) and after (b, c) corrosion in 0.5 MPa CO2 saturated 3.5%NaCl solutions without (b) and with (c) CTLY
Fig.10  3D-AFM surface micrographs of Q235 steel before (a) and after (b, c) corrosion in 0.5 MPa CO2 saturated 3.5%NaCl solutions without (b) and with (c) CTLY
SampleRa / nmRq / nmRmax / nm
Before corrosion25.233.7257.7
After corrosion (without CTLY)124.2153.6990.4
After corrosion (with CTLY)22.431.4212.2
Table 6  AFM determined surface roughnesses of Q235 steel based on the results in Fig.10
Fig.11  XRD patterns of Q235 steel after corrosion in 0.5 MPa CO2 saturated 3.5%NaCl solutions with (a) and without (b) CTLY
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