Selective removal of arsenate from drinking water using a polymeric ligand exchanger

被引:147
作者
An, B [1 ]
Steinwinder, TR [1 ]
Zhao, DY [1 ]
机构
[1] Auburn Univ, Dept Civil Engn, Harbert Engn Ctr 238, Environm Engn Program, Auburn, AL 36849 USA
关键词
arsenate; arsenic; ion exchange; ligand exchange; regeneration; sorption;
D O I
10.1016/j.watres.2005.10.014
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The new maximum contaminant level (MCL) of 10 mu g/L for arsenic in the US drinking water will take effect on January 22, 2006. The compliance cost is estimated to be similar to$ 600 million per year using current treatment technologies. This research aims to develop an innovative ion exchange process that may help water utilities comply with the new MCL in a more cost-effective manner. A polymeric ligand exchanger (PLE) was prepared by loading Cu2+ to a commercially available chelating ion exchange resin. Results from batch and column experiments indicated that the PLE offered unusually high selectivity for arsenate over other ubiquitous anions such as sulfate, bicarbonate and chloride. The average binary arsenate/sulfate separation factor for the PLE was determined to be 12, which were over two orders of magnitude greater than that (0.1-0.2) for commercial strong-base anion (SBA) exchangers. Because of the enhanced arsenate selectivity, the PLE was able to treat similar to 10 times more bed volumes (BVs) of water than commonly used SBA resins. The PLE can operate optimally in the neutral pH range (6.0-8.0). The exhausted PLE can be regenerated highly efficiently. More than 95% arsenate capacity can be recovered using similar to 22 BVs of 4% (w/w) NaCl at pH 9.1, and the regenerated PLE can be reused without any capacity drop. Upon treatment using FeCl3,, the spent brine was recovered and reused for regeneration, which may cut down the regenerant need and reduces the volume of process waste residuals. The PLE can be used as a highly selective and reusable sorbent for removal of arsenate from drinking water. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4993 / 5004
页数:12
相关论文
共 48 条
[1]  
[Anonymous], 2001, PR NEWSWIRE
[2]  
[Anonymous], EPA600R00088 OFF RES
[3]   Intraparticle diffusion and adsorption of arsenate onto granular ferric hydroxide (GFH) [J].
Badruzzaman, M ;
Westerhoff, P ;
Knappe, DRU .
WATER RESEARCH, 2004, 38 (18) :4002-4012
[4]   Arsenic(V) removal with polymer inclusion membranes from sulfuric acid media using DBBP as carrier [J].
Ballinas, MD ;
De San Miguel, ER ;
Rodríguez, MTD ;
Silva, O ;
Muñoz, M ;
De Gyves, J .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2004, 38 (03) :886-891
[5]   Sorption and filtration of metals using iron-oxide-coated sand [J].
Benjamin, MM ;
Sletten, RS ;
Bailey, RP ;
Bennett, T .
WATER RESEARCH, 1996, 30 (11) :2609-2620
[6]   Alternative methods for membrane filtration of arsenic from drinking water [J].
Brandhuber, P ;
Amy, G .
DESALINATION, 1998, 117 (1-3) :1-10
[7]   LIGAND-EXCHANGE SORPTION OF ARSENATE AND ARSENITE ANIONS BY CHELATING RESINS IN FERRIC ION FORM .2. IMINODIACETIC CHELATING RESIN CHELEX-100 [J].
CHANDA, M ;
ODRISCOLL, KF ;
REMPEL, GL .
REACTIVE POLYMERS, 1988, 8 (01) :85-95
[8]  
Chen HW, 1999, J AM WATER WORKS ASS, V91, P74
[9]  
Chwirka JD, 2004, J AM WATER WORKS ASS, V96, P106
[10]  
CLIFFORD D, 1991, ION EXCHANGE INORGAN