Electrochemical Corrosion Behavior and Mechanism of X80 Steel in the Aqueous Solution of Carbon Dioxide
摘 要
在模拟油田采出水腐蚀环境中, 采用电化学交流阻抗和动电位扫描极化曲线测试技术, 研究了X80钢在温度为60 ℃, 饱和CO2条件下的腐蚀电化学行为和阳极与阴极的反应机理, 实时监测了腐蚀产物膜对腐蚀行为和腐蚀反应机理的影响。研究结果表明: X80钢的阳极反应过程服从Bockris机理; X80钢的阴极反应以H2CO3的还原为主; 反应中间产物吸附与腐蚀产物膜覆盖的竞争导致交流阻抗谱随腐蚀时间而变化, 影响着钢的腐蚀行为;产物膜对钢基体具有一定的保护作用。
Abstract
The corrosion environment in oil produced water was simulated in the solution saturated with CO2, and the electrochemical corrosion behavior of X80 steel and the reaction mechanisms in anode and cathode at 60 ℃ were studied by means of electrochemical impendence spectroscopy(EIS) and potentialydynamic polarization curve. The effects of corrosion product film on the corrosion behavior and the corrosion reaction mechanism were monitored. The results showed that the anodic reactions obey Bockris mechanism, the predominant cathodic reaction is the reduction of carbonic acid, the competition between the deposition of corrosion product and the adsorption of reaction intermediate product influences the corrosion behavior of X80 steel and leads to the variation of EIS with corrosion time. The corrosion product film prevents X80 steel from further corrosion.
中图分类号 TG172 TG174.3
所属栏目 试验研究
基金项目 国家科技支撑计划项目(2006BAB03B05)
收稿日期 2011/1/2
修改稿日期 2011/2/25
网络出版日期
作者单位点击查看
备注魏爱军, 高级工程师,
引用该论文: WEI Ai-jun,HUO Fu-yong,JIANG Hua-yi. Electrochemical Corrosion Behavior and Mechanism of X80 Steel in the Aqueous Solution of Carbon Dioxide[J]. Corrosion & Protection, 2011, 32(12): 933
被引情况:
【1】王霞,吴红梅,吴艺琛,韩丽丹,彭波, "管线钢X65和X70在含饱和CO2采出水中的腐蚀行为",腐蚀与防护 35, 657-661(2014)
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参考文献
【1】Linter B R, Burstein G T. Reaction of pipeline steels in carbon dioxide solutions[J]. Corrosion Science, 1999, 42(2):117-120.
【2】Davies D H, Burstein G T. The effect s of bicarbonate on the corrosion and passivation of iron[J]. Corrosion, 1980, 36(8):416-419.
【3】Ogundele G I, White W E. Some observation on corrosion of carbon steel in aqueous environments containing carbon dioxide[J]. Corrosion, 1986, 42(2):71-75.
【4】Videm K. In predicting CO2 corrosion in the oil and gas industry[C]. London U K:Institute of Materials, 1994:134-137.
【5】Bockris J O M, Drazic D, Despic A R. The electrode kinetics of the deposition and dissolution of iron[J]. Electrochim Acta, 1961, 4(4):325-328.
【6】曹楚南. 混合电位下的法拉第导纳[J]. 中国腐蚀与防护学报, 1993, 13(2):91-100.
【7】王佳, 曹楚南. 缓蚀剂阳极脱附现象的研究Ⅱ 缓蚀剂阳极脱附对电极阻抗的影响[J]. 中国腐蚀与防护学报, 1995, 15(4):247-253.
【8】曹楚南, 张鉴清. 电化学阻抗谱导论[M]. 北京:科学出版社, 2002.
【9】王佳, 曹楚南, 林海潮. 孔蚀发展期的电极阻抗频谱特征[J]. 中国腐蚀与防护学报, 1989, 9(4):271-279.
【10】曾潮流, 王文, 吴维文 山. 熔融盐热腐蚀的电化学阻抗模型[J]. 金属学报, 1999, 35(7):751-754.
【11】Nesic S, Postlet Hwaite J, Olsen S. An electrochemical model for prediction of corrosion of mild steel in aqueous carbon dioxide solutions[J]. Corrosion, 1996, 52(4):280-283.
【12】刘烈炜, 胡倩, 彭建雄, 等. 中性水介质中碳钢CO2腐蚀碳钢与表面膜结构关系[J]. 材料保护, 2001, 34(1):6-7, 21.
【2】Davies D H, Burstein G T. The effect s of bicarbonate on the corrosion and passivation of iron[J]. Corrosion, 1980, 36(8):416-419.
【3】Ogundele G I, White W E. Some observation on corrosion of carbon steel in aqueous environments containing carbon dioxide[J]. Corrosion, 1986, 42(2):71-75.
【4】Videm K. In predicting CO2 corrosion in the oil and gas industry[C]. London U K:Institute of Materials, 1994:134-137.
【5】Bockris J O M, Drazic D, Despic A R. The electrode kinetics of the deposition and dissolution of iron[J]. Electrochim Acta, 1961, 4(4):325-328.
【6】曹楚南. 混合电位下的法拉第导纳[J]. 中国腐蚀与防护学报, 1993, 13(2):91-100.
【7】王佳, 曹楚南. 缓蚀剂阳极脱附现象的研究Ⅱ 缓蚀剂阳极脱附对电极阻抗的影响[J]. 中国腐蚀与防护学报, 1995, 15(4):247-253.
【8】曹楚南, 张鉴清. 电化学阻抗谱导论[M]. 北京:科学出版社, 2002.
【9】王佳, 曹楚南, 林海潮. 孔蚀发展期的电极阻抗频谱特征[J]. 中国腐蚀与防护学报, 1989, 9(4):271-279.
【10】曾潮流, 王文, 吴维文 山. 熔融盐热腐蚀的电化学阻抗模型[J]. 金属学报, 1999, 35(7):751-754.
【11】Nesic S, Postlet Hwaite J, Olsen S. An electrochemical model for prediction of corrosion of mild steel in aqueous carbon dioxide solutions[J]. Corrosion, 1996, 52(4):280-283.
【12】刘烈炜, 胡倩, 彭建雄, 等. 中性水介质中碳钢CO2腐蚀碳钢与表面膜结构关系[J]. 材料保护, 2001, 34(1):6-7, 21.
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