Understanding soluble arsenate removal kinetics by zerovalent iron media

被引:106
作者
Melitas, N
Wang, JP
Conklin, M
O'Day, P
Farrell, J [1 ]
机构
[1] Univ Arizona, Dept Chem & Environm Engn, Tucson, AZ 85721 USA
[2] Univ Arizona, Dept Hydrol & Water Resources, Tucson, AZ 85721 USA
[3] Arizona State Univ, Dept Geol Sci, Tempe, AZ 85287 USA
关键词
D O I
10.1021/es011250y
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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 μg/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 μg/L resulted in no further decrease in the iron corrosion rate. The kinetics of arsenate removal ranged between zeroth- and first-order with respectto 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.
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页码:2074 / 2081
页数:8
相关论文
共 41 条
[1]  
ALAUDDIN M, 2000, P 4 INT C ARS EXP HL
[2]   KINETICS OF THE HYDROGEN EVOLUTION REACTION ON MILD-STEEL AND NICKEL CATHODES IN CONCENTRATED SODIUM-HYDROXIDE SOLUTIONS [J].
BROWN, AP ;
KRUMPELT, M ;
LOUTFY, RO ;
YAO, NP .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1982, 129 (11) :2481-2487
[3]  
Cornell R. M., 1996, The Iron Oxides
[4]   Granular ferric hydroxide - a new adsorbent for the removal of arsenic from natural water [J].
Driehaus, W ;
Jekel, M ;
Hildebrandt, U .
JOURNAL OF WATER SERVICES RESEARCH AND TECHNOLOGY-AQUA, 1998, 47 (01) :30-35
[5]  
EPA, 2001, National primary drinking water regulations
[6]  
arsenic and clarifications to compliance and new source contaminants monitoring. In: Final Rule, V66, P6976
[7]   Electrochemical and spectroscopic study of arsenate removal from water using zero-valent iran media [J].
Farrell, J ;
Wang, JP ;
O'Day, P ;
Conklin, M .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2001, 35 (10) :2026-2032
[8]   Arsenate and chromate retention mechanisms on goethite .1. Surface structure [J].
Fendorf, S ;
Eick, MJ ;
Grossl, P ;
Sparks, DL .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 1997, 31 (02) :315-320
[9]   SURFACE-CHEMISTRY OF FERRIHYDRITE .2. KINETICS OF ARSENATE ADSORPTION AND COPRECIPITATION [J].
FULLER, CC ;
DAVIS, JA ;
WAYCHUNAS, GA .
GEOCHIMICA ET COSMOCHIMICA ACTA, 1993, 57 (10) :2271-2282
[10]  
George G.N., 1993, EXAFSPAK SUITE COMPU