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Effect of Flow Velocity and Carbon Chain Length on Corrosion Inhibition Performance of Imidazoline Derivates in High Pressure CO2 Environment |
ZHAO Tong1, ZHAO Jingmao1,2( ), JIANG Ruijing1,2 |
1. College of Material Science and Engineering, Beijing University of Chemical Technology, Beijing 100029, China 2. Beijing Key Laboratory of Electrochemical Process and Technology for Materials, Beijing University of Chemical Technology, Beijing 100029, China |
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Abstract Five imidazoline derivates with different carbon chain length and two imidazoline derivates with double bond in carbon chain were synthesized. Their inhibition performance, adsorption capacity and hydrophobicity were studied in high CO2 pressured solution by means of dynamic mass loss method, SEM, AFM, and contact angle measurement. By contact angle measurement, it was found that the hydrophobic performance of imidazoline derivate with 21 carbon chain length was the best, and the contact angle was 80.5°, 87.8° and 96.2° respectively corresponding to its concentration of 50, 100 and 200 mg/L. By the AFM force curves, it was also found that the longer the carbon chain, the larger the adhesion force. When the chain length was 21, the adhesion reached the highest. The dynamic weight loss experiment showed that the inhibition performance of the imidazoline derivates was related to both the chain length and the flow velocity of the solution. When the flow rate was 0.3 and 0.6 m/s, the derivate with 17 carbons in carbon chain was the best and when the flow rate was 5.5 m/s, the longer the carbon chain of imidazoline, the better the inhibition performance. The inhibition performance of imidazoline with double bonds in carbon chain was always better than the one without double bonds under the same condition.
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Received: 19 May 2014
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[1] |
Nesic S. Key issues related to modelling of internal corrosion of oil and gas pipelines-A review[J]. Corros. Sci., 2007, 49: 4308
|
[2] |
Zhao G X, Yan M L, Chen C F, et al. Studies on influence factors of CO2 corrosion rate[J]. Oil Field Equip., 2001, 30: 72
|
|
(赵国仙, 严密林, 陈长风等. 影响碳钢CO2腐蚀速率因素的研究[J]. 石油矿场机械, 2001, 30: 72)
|
[3] |
Sun L, Li C J, Peng S B, et al. Research of the effceting factors of CO2 corrosion[J]. Pipeline Tech. Equip., 2008, 6: 35
|
|
(孙丽, 李长俊, 彭善碧等. CO2腐蚀影响因素研究[J]. 管道技术与设备, 2008, 6: 35)
|
[4] |
Suzuki K, Kouno T, Eiji S, et al. The study of inhibitor for sour gas service[J]. Corrosion, 1982, 38(7): 384
|
[5] |
Ramachandran S, Tsai B L, Blanco M, et al. Self-assembled monolayer mechanism for corrosion inhibition of iron by imidazolines[J]. Langmuir, 1996, 12(26): 6419
|
[6] |
Jovancicevic V, Ramachandran S, Prince P. Inhibition of carbon dioxide corrosion of mild steel by imidazolines and their precursors[J]. Corrosion, 1999, 55(5): 449
|
[7] |
Sun M Q, Ge J J, Zhang G C, et al. Relationship between molecular structure of imidazoline and its corrosion inhibition performance in salty solution with saturated CO2[J]. Petrochem. Technol., 2005, 34(12): 1177
|
|
(孙铭勤, 葛际江, 张贵才等. 饱和CO2盐水中咪唑啉分子结构与其缓蚀性能的关系[J]. 石油化工, 2005, 34(12): 1177)
|
[8] |
Yang H Y, Chen J J, Cao C N, et al. Study on corrosion and inhibition mechanism in H2S aqueous solutions VI: The relationship between molecular structure of imidazoline derivatives and inhibition performance in H2S solutions[J]. J. Chin. Soc. Corros. Prot., 2002, 22(3): 148
|
|
(杨怀玉, 陈家坚, 曹楚南等. H2S水溶液中的腐蚀与缓蚀作用机理的研究VI: H2S溶液中咪唑啉衍生物分子结构与其缓蚀性能的关系[J]. 中国腐蚀与防护学报, 2002, 22(3): 148)
|
[9] |
Liu X, Zheng Y G. The effect of hydrophobic group on the inhibition behavior of imidazoline for CO2 corrosion of N80 in 3%NaCl solution[J]. J. Chin. Soc. Corros. Prot., 2009, 29(5): 333
|
|
(刘瑕, 郑玉贵. 咪唑啉型缓蚀剂中疏水基团对N80钢在CO2饱和的3%NaCl溶液中的缓蚀性能影响[J]. 中国腐蚀与防护学报, 2009, 29(5): 333)
|
[10] |
Zhang J, Liu J X, Yu W Z, et al. Molecular modeling of the inhibition mechanism of 1-(2-aminoethyl)-2-alkyl-imidazoline[J]. Corros. Sci., 2010, 52(6): 2059
|
[11] |
Bommersbach P, Alemany-Dumont C, Millet J P, et al. Formation and behaviour study of an environment-friendly corrosion inhibitor by electrochemical methods[J]. Electrochim. Acta, 2005, 51(6): 1076
|
[12] |
Ochoa N, Moran F, Pébère N, et al. Influence of flow on the corrosion inhibition of carbon steel by fatty amines in association with phosphonocarboxylic acid salts[J]. Corros. Sci., 2005, 47(3): 593
|
[13] |
Srisuwan N, Ochoa N, Pébère N, et al. Variation of carbon steel corrosion rate with flow conditions in the presence of an inhibitive formulation[J]. Corros. Sci., 2008, 50(5): 1245
|
[14] |
Edwards A, Osborne C, Webster S, et al. Mechanistic studies of the corrosion inhibitor oleic imidazoline[J]. Corros. Sci., 1993, 36(2): 315
|
[15] |
Ortega-Toledoa D M, Gonzalez-Rodriguezb J G, Casales M, et al. CO2 corrosion inhibition of X-120 pipeline steel by a modified imidazoline under flow conditions[J]. Corros. Sci., 2011, 53(11):3780
|
[16] |
Jiang X, Zheng Y G, Ke W. Effect of flow velocity and entrained sand on inhibition performances of two inhibitors for CO2 corrosion of N80 steel in 3%NaCl solution[J]. Corros. Sci., 2005, 47(11): 2636
|
[17] |
Zhang Z. Development of supramolecular corrosion inhibitor and its protective effect on condensate system [D]. Beijing: Beijing University of Chemical Technology, 2013
|
|
(张展. 超分子缓蚀剂对凝结水系统的保护 [D]. 北京: 北京化工大学, 2013)
|
[18] |
Qu J E, Guo X P, Huang J Y, et al. Study on adsorption behavior of inhibitors by electrochemical metheods and AFM force curves[J]. J. Instrum. Anal., 2007, 26(1): 110
|
|
(屈钧娥, 郭兴蓬, 黄金营等. 缓蚀剂吸附行为的电化学及AFM力曲线研究[J]. 分析测试学报, 2007, 26(1): 110)
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