Chen Jukai, Wang Xiaodan, Ma Honglian, Huo Zhiyuan, Wang Yueshe
School of Chemical Engineering & Technology, China University of Mining and Technology, No. 1, Daxue Road, Xuzhou, Jiangsu 221116, China.
State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, No. 28, West Xianning Road, Xi'an, Shaanxi 710049, China.
ACS Omega. 2022 Feb 8;7(7):6142-6150. doi: 10.1021/acsomega.1c06613. eCollection 2022 Feb 22.
A combined steady-state and transient approach is employed to investigate the corrosion behavior of X80 pipeline steel in carbon dioxide-saturated brines. Continuous bubbling of carbon dioxide into a test vessel with 1 liter capacity is performed to simulate the flowing condition. The measurement of time-dependent open-circuit potential, polarization resistance, and electrochemical impedance spectroscopy (EIS) is conducted to interpret the evolution of dissolution processes at the corroding interface. Three distinguishing stages are observed at a temperature of 60 °C during a whole exposure of 144 h. Analyses mainly based on the consecutive mechanism show that after the first stage of the active-adsorption state, the anodic reaction is significantly retarded by the accumulation of (FeOH) on the iron surface, causing a sharp increase in the polarization resistance and the open-circuit potential, as well as the disappearance of the inductive loop in EIS. At the third stage, the formation of the corrosion product layer similarly reduces both the anodic and cathodic reactions, which arouses a linear increase in the polarization resistance with time and a capacitive loop in EIS but changes the open-circuit potential slightly. An increase in salinity in this study reduces the polarization resistance and enhances iron dissolution by promoting the formation and relaxation of (FeOH); however, it brings little change to the developing time of the three stages obviously. At a low temperature of 20 °C, a protective product layer is not observed in carbon dioxide-saturated brine, and the dissolution of iron is mainly under activation control during the whole exposure. A notable enlarged polarization resistance and different interfacial processes are observed in an alkaline solution compared with those in acidic environments, which is deduced to be resulted from an impedance in the relaxation of (FeOH) by increasing pH. The observations in this study support well that the iron dissolution reaction at the initial stage exposed in carbon dioxide aqueous environments is dominant by water adsorption on the iron surface, and further investigation should be performed on the role that carbon dioxide plays in the evolution of corrosion products and the formation of a protective film on the steel surface by taking into account local water chemistry.
采用稳态和瞬态相结合的方法研究了X80管线钢在二氧化碳饱和盐水中的腐蚀行为。向容量为1升的测试容器中持续通入二氧化碳气泡以模拟流动条件。通过测量随时间变化的开路电位、极化电阻和电化学阻抗谱(EIS)来解释腐蚀界面处溶解过程的演变。在60℃的温度下,经过144小时的全暴露过程,观察到三个不同阶段。基于连续机理的分析表明,在活性吸附状态的第一阶段之后,铁表面(FeOH)的积累显著阻碍了阳极反应,导致极化电阻和开路电位急剧增加,同时EIS中感应环消失。在第三阶段,腐蚀产物层的形成同样降低了阳极和阴极反应,导致极化电阻随时间线性增加,EIS中出现电容环,但开路电位变化较小。本研究中盐度的增加降低了极化电阻,并通过促进(FeOH)的形成和弛豫增强了铁的溶解;然而,它对三个阶段的发展时间没有明显影响。在20℃的低温下,在二氧化碳饱和盐水中未观察到保护性产物层,并且在整个暴露过程中铁的溶解主要受活化控制。与酸性环境相比,在碱性溶液中观察到极化电阻显著增大且界面过程不同,这被推断是由于pH值升高导致(FeOH)弛豫受阻。本研究中的观察结果很好地支持了在二氧化碳水环境中暴露初期铁的溶解反应主要由铁表面的水吸附主导,并且应进一步研究二氧化碳在腐蚀产物演变以及钢表面保护膜形成过程中所起的作用,同时考虑局部水化学情况。