Arsenic removal from water by hybrid electro-regenerated anion exchange resin/electrodialysis process

被引:87
|
作者
Ortega, Arturo [1 ,2 ]
Oliva, Irazema [2 ]
Contreras, Kenia E. [2 ]
Gonzalez, Ignacio [3 ]
Cruz-Diaz, Martin R. [2 ]
Rivero, Eligio P. [2 ]
机构
[1] Univ Nacl Autonoma Mexico, Fac Quim, Av Univ 3000, Ciudad De Mexico 04510, DF, Mexico
[2] Univ Nacl Autonoma Mexico, Fac Estudios Super Cuautitlan, Dept Ingn & Tecnol, Av 1 Mayo, Cuautitlan 54740, Estado De Mexic, Mexico
[3] Univ Autonoma Metropolitana Iztapalapa, Dept Quim, San Rafael Atlixco186, Mexico City 09340, DF, Mexico
关键词
Ion exchange/electrodialysis; Arsenic removal; Resin regeneration; Anion exchange membrane; Water splitting; WASTE-WATER; ELECTRODEIONIZATION; RECOVERY; SYSTEM; IONS;
D O I
10.1016/j.seppur.2017.04.050
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
One of the major public health concerns worldwide is arsenic presence in the water intended for human consumption in different countries. This paper proposes the use of the hybrid ion exchange/electrodialysis (IXED) process for arsenic removal from water. Its objective is to lower the concentration of dilute solutions of As(V) ions to values below the maximum limit (10 mu g L-1 As) recommended by the World Health Organization. To prove this method, a 5-compartmentcell was used: a central compartment filled with anion exchange resin and delimited by anion exchange membranes, two adjacent compartments with cationic membranes on the ends and two rinse compartments, one at each electrode. Ion exchange/electrodialysis process was performed as a batch wise operation by recirculating arsenic solutions through the central compartment and the two adjacent compartments. The As(V) ions in the solution are exchanged by OH- in the resin which is regenerated with OH- ions produced by water dissociation at the membrane-electrolyte interface, according to changes in pH, conductivity and As concentration in each compartment. The obtained results show that IXED is capable of removing arsenic from solutions at different concentrations ranging between 2.1 and 15 mg L-1 As, until reaching the final concentration <= 10 mu g L-1 with a current efficiency between 8.2 and 47.7% and energy consumption between 7.5 and 63.9 kW h per kg of removed As(V). (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:319 / 326
页数:8
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