Melitas Nikos, Wang Jianping, Conklin Martha, O'Day Peggy, Farrell James
Department of Chemical and Environmental Engineering, University of Arizona, Tucson 85721, USA.
Environ Sci Technol. 2002 May 1;36(9):2074-81. doi: 10.1021/es011250y.
Zerovalent iron filings have been proposed as a filter medium for removing arsenic compounds from potable water supplies. This research investigated the kinetics of arsenate removal from aqueous solutions by zerovalent iron media. Batch experiments were performed to determine the effect of the iron corrosion rate on the rate of As(V) removal. Tafel analyses were used to determine the effect of the As(V) concentration on the rate of iron corrosion in anaerobic solutions. As(V) removal in column reactors packed with iron filings was measured over a 1-year period of continuous operation. Comparison of As(V) removal by freely corroding and cathodically protected iron showed that rates of arsenate removal were dependent on the continuous generation of iron oxide adsorption sites. In addition to adsorption site availability, rates of arsenate removal were also limited by mass transfer associated with As(V) diffusion through iron corrosion products. Steady-state removal rates in the column reactor were up to 10 times faster between the inlet-end and the first sampling port than between the first sampling port and the effluent-end of the column. Faster removal near the influent-end of the column was due to a faster rate of iron oxidation in that region. The presence of 100 microg/L As(V) decreased the iron corrosion rate by up to a factor of 5 compared to a blank electrolyte solution. However, increasing the As(V) concentration from 100 to 20,000 microg/L resulted in no further decrease in the iron corrosion rate. The kinetics of arsenate removal ranged between zeroth- and first-order with respect to the aqueous As(V) concentration. The apparent reaction order was dependent on the availability of adsorption sites and on the aqueous As(V) concentration. X-ray absorption spectroscopy analyses showed the presence of iron metal, magnetite (Fe3O4), an Fe(III) oxide phase, and possibly an Fe(II,III) hydroxide phase in the reacted iron filings. These mixed valent oxide phases are not passivating and permit sustained iron corrosion and continuous generation of new sites for As(V) adsorption.
零价铁屑已被提议作为一种过滤介质,用于从饮用水供应中去除砷化合物。本研究调查了零价铁介质从水溶液中去除砷酸盐的动力学。进行了批量实验,以确定铁腐蚀速率对As(V)去除率的影响。采用塔菲尔分析来确定As(V)浓度对厌氧溶液中铁腐蚀速率的影响。在连续运行1年的时间内,测量了填充铁屑的柱式反应器中As(V)的去除情况。比较自由腐蚀和阴极保护铁对As(V)的去除情况表明,砷酸盐的去除速率取决于氧化铁吸附位点的持续生成。除了吸附位点的可用性外,砷酸盐的去除速率还受到与As(V)通过铁腐蚀产物扩散相关的传质限制。柱式反应器中稳态去除速率在进水端和第一个采样口之间比在第一个采样口和柱式反应器出水端之间快高达10倍。柱式反应器进水端附近去除速度更快是由于该区域铁氧化速率更快。与空白电解质溶液相比,100μg/L As(V)的存在使铁腐蚀速率降低了高达5倍。然而,将As(V)浓度从100μg/L提高到20,000μg/L并没有导致铁腐蚀速率进一步降低。砷酸盐去除动力学在零级和一级之间,取决于水溶液中As(V)浓度。表观反应级数取决于吸附位点的可用性和水溶液中As(V)浓度。X射线吸收光谱分析表明,反应后的铁屑中存在铁金属、磁铁矿(Fe3O4)、一种Fe(III)氧化物相,以及可能的一种Fe(II,III)氢氧化物相。这些混合价态的氧化物相不会钝化,允许持续的铁腐蚀和持续产生新的As(V)吸附位点。