Iron-modified light expanded clay aggregates for the removal of arsenic(V) from groundwater

被引:57
作者
Haque, Namul [1 ,2 ]
Morrison, Gregory [1 ,2 ]
Cano-Aguilera, Irene [3 ]
Gardea-Torresdey, Jorge L. [3 ,4 ]
机构
[1] Univ Texas El Paso, Environm Sci & Engn PhD Program, El Paso, TX 79968 USA
[2] Chalmers Univ Technol, SE-41296 Gothenburg, Sweden
[3] Univ Guanajuato, Fac Quim, Guanajuato 36050, Mexico
[4] Univ Texas El Paso, Dept Chem, El Paso, TX 79968 USA
基金
美国国家卫生研究院;
关键词
arsenic; adsorbent; kinetics; isotherms; flow experiments;
D O I
10.1016/j.microc.2007.08.004
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Iron modified materials have been proposed as a filter medium to remove arsenic compounds from groundwater. This research investigated the removal of arsenate, As(V) from aqueous solutions by iron-coated light expanded clay aggregates (Fe-LECA). Arsenic is effectively adsorbed by Fe-LECA in the optimum pH range 6-7 by using a 10 mg mL(-1) adsorbent dose. Kinetics experiments were performed to investigate the adsorption mechanisms. Electrostatic attraction and surface complexation were proposed to be the major arsenic removal mechanisms. The experimental data fitted the pseudo-first-order equation of Lagergren. For an arsenic concentration of 1 mg L-1, the rate constant (k(1)) of pseudo-first-order was 0.098 min(-1), representing a rapid adsorption in order to reach equilibrium early. Equilibrium sorption isotherms were constructed from batch sorption experiments and the data was best described by the Langmuir isotherm model. Large scale column experiments were conducted under different bed depths, flow rates, coating duration and initial iron salts concentration to determine the optimal arsenic removal efficiency by Fc-LECA column. Volumetric design as well as higher hydraulic detention time was proposed to optimize the efficiency of the column to remove arsenic. In addition, concentrated iron salts and longer coating duration were also found to be crucial parameters for arsenic removal. The maximum arsenic accumulation was 3.31 mg of As g(-1) of Fe-LECA when the column was operated at a flow rate of 10 mL min(-1) and the LECA was coated with 0.1 M FeCl3 suspension for a 24 h coating duration. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:7 / 13
页数:7
相关论文
共 45 条
[1]  
Altundogan HS, 2000, WASTE MANAGE, V20, P761
[2]   Selective removal of arsenate from drinking water using a polymeric ligand exchanger [J].
An, B ;
Steinwinder, TR ;
Zhao, DY .
WATER RESEARCH, 2005, 39 (20) :4993-5004
[3]   Removal of arsenic from water by zero-valent iron [J].
Bang, S ;
Korfiatis, GP ;
Meng, XG .
JOURNAL OF HAZARDOUS MATERIALS, 2005, 121 (1-3) :61-67
[4]   Chemical reactions between arsenic and zero-valent iron in water [J].
Bang, S ;
Johnson, MD ;
Korfiatis, GP ;
Meng, XG .
WATER RESEARCH, 2005, 39 (05) :763-770
[5]   Effects of iron on arsenic speciation and redox chemistry in acid mine water [J].
Bednar, AJ ;
Garbarino, JR ;
Ranville, JF ;
Wildeman, TR .
JOURNAL OF GEOCHEMICAL EXPLORATION, 2005, 85 (02) :55-62
[6]   Arsenic calamity in the Indian subcontinent - What lessons have been learned? [J].
Chakraborti, D ;
Rahman, MM ;
Paul, K ;
Chowdhury, UK ;
Sengupta, MK ;
Lodh, D ;
Chanda, CR ;
Saha, KC ;
Mukherjee, SC .
TALANTA, 2002, 58 (01) :3-22
[7]   Sorption materials for arsenic removal from water: A comparative study [J].
Daus, B ;
Wennrich, R ;
Weiss, H .
WATER RESEARCH, 2004, 38 (12) :2948-2954
[8]   Sorption of As(V) ions by akaganeite-type nanocrystals [J].
Deliyanni, EA ;
Bakoyannakis, DN ;
Zouboulis, AI ;
Matis, KA .
CHEMOSPHERE, 2003, 50 (01) :155-163
[9]   THE OXIDATION-STATES OF ARSENIC IN WELL-WATER FROM A CHRONIC ARSENICISM AREA OF NORTHERN MEXICO [J].
DELRAZO, LM ;
ARELLANO, MA ;
CEBRIAN, ME .
ENVIRONMENTAL POLLUTION, 1990, 64 (02) :143-153
[10]   Removal of As(III) and As(V) from water using a natural Fe and Mn enriched sample [J].
Deschamps, E ;
Ciminelli, VST ;
Höll, WH .
WATER RESEARCH, 2005, 39 (20) :5212-5220