Melitas Nikos, Farrell James
Department of Chemical and Environmental Engineering, University of Arizona, Tucson, Arizona 85721, USA.
Environ Sci Technol. 2002 Dec 15;36(24):5476-82. doi: 10.1021/es0258071.
The kinetics of chromate removal from contaminated water by zerovalent iron media are not well understood. This study investigated the reactions occurring on iron surfaces in chromate solutions in order to understand the removal kinetics and to assess the long-term ability of zerovalent iron for removing Cr(VI) from contaminated water. Tafel polarization analysis and electrochemical impedance spectroscopy were used to determine the corrosion rates and charge-transfer resistances associated with Cr(VI) removal by iron wires suspended in electrolyte solutions with initial Cr(VI) concentrations of 10,000 microg/L. The condition of the iron surfaces at the time of their exposure to chromate determined the effectiveness of the iron for chromate removal. Both iron coated with a water-formed oxide and initially oxide-free iron were effective for chromate removal. However, iron coated with an air-formed oxide was an order of magnitude less effective for removing soluble chromium. Although iron with the air-formed oxide was largely passivated with respect to chromate removal, its overall rate of corrosion was similar to that for iron with the other initial surface conditions. This indicates that water, but not chromate, was able to penetrate the air-formed oxide coating and access cathodic sites. For all initial surface conditions, addition of chromate decreased the corrosion rate by increasing the corrosion potential and the anodic charge transfer resistance. Although Cr(VI) is a strong oxidant rates of iron corrosion were not proportional to the aqueous Cr(VI) concentrations due to anodic control of iron corrosion. Under anodically controlled conditions, the rate of corrosion was limited by the rate at which Fe2+ could be released at anodic sites and not by the rate at which oxidants were able to accept electrons. This study shows that the zero order removal kinetics of Cr(VI) by iron media can be explained by anodic control of iron corrosion and the concomitant anodic control of Cr(VI) reduction.
零价铁介质从受污染水中去除铬酸盐的动力学尚未得到充分理解。本研究调查了铬酸盐溶液中铁表面发生的反应,以了解去除动力学,并评估零价铁从受污染水中去除Cr(VI)的长期能力。采用塔菲尔极化分析和电化学阻抗谱来确定与悬浮在初始Cr(VI)浓度为10,000μg/L的电解质溶液中的铁丝去除Cr(VI)相关的腐蚀速率和电荷转移电阻。铁表面暴露于铬酸盐时的状态决定了铁去除铬酸盐的有效性。涂有水生成氧化物的铁和初始无氧化物的铁对铬酸盐去除均有效。然而,涂有空气生成氧化物的铁去除可溶性铬的效率要低一个数量级。尽管涂有空气生成氧化物的铁在去除铬酸盐方面基本处于钝化状态,但其总体腐蚀速率与其他初始表面条件的铁相似。这表明水而非铬酸盐能够穿透空气生成的氧化物涂层并到达阴极部位。对于所有初始表面条件,添加铬酸盐会通过提高腐蚀电位和阳极电荷转移电阻来降低腐蚀速率。尽管Cr(VI)是一种强氧化剂,但由于铁腐蚀的阳极控制,铁的腐蚀速率与水溶液中Cr(VI)的浓度不成正比。在阳极控制条件下,腐蚀速率受Fe2+在阳极部位释放速率的限制,而不是受氧化剂接受电子速率的限制。本研究表明,铁介质对Cr(VI)的零级去除动力学可以通过铁腐蚀的阳极控制以及伴随的Cr(VI)还原的阳极控制来解释。