Membrane-based hybrid processes for high water recovery and selective inorganic pollutant separation

被引:75
作者
Ritchie, SMC [1 ]
Bhattacharyya, D [1 ]
机构
[1] Univ Kentucky, Dept Chem & Mat Engn, Lexington, KY 40506 USA
关键词
hybrid processes; membranes; sorption; inorganics;
D O I
10.1016/S0304-3894(01)00370-3
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The removal of heavy metals (e.g. Pb(II), Cd(II), Cu(II), etc.) and oxyanions (e.g. nitrate, AS(III, V), Cr(VI), etc.) is of immense interest for treatment of groundwater and other dilute aqueous systems. However, the presence of non-toxic components, such as hardness (Ca, Mg) and sulfate, can interfere with the separation of toxic species. For example, pressure-driven membrane processes, such as reverse osmosis (RO), have been limited for water treatment due to problems that these extraneous components cause with water recovery and ionic strength (osmotic pressure) of the retentate. In addition, nitrate rejection by RO is considerably lower than NaCl rejection, resulting in permeate concentrations that may be too high for groundwater recharging. Other separation systems that rely solely on sorption of toxic species (e.g. ion exchange resins) may not have sufficient selectivity for efficient use in the presence of competing ions. Hence, implementation of pressure-driven membrane separations and high capacity sorbents in hybrid processes shows much promise for remedying these difficulties. For example, selective separation of nitrate may be achieved by combining nanofiltration (NF) for sulfate removal, followed by RO or ion exchange for nitrate removal (see example 1). When small concentrations of toxic metals are present, the large retentate volumes of RO processes may be reduced by selective removal of toxic species with a high capacity sorbent, thus permitting disposal of a lower volume, non-toxic stream (see example 2). The use of microfiltration membrane-based sorbents containing multiple polymeric functional groups is a novel technique to achieve high metal sorption capacity under convective flow conditions. These sorbents are formed by the attachment of various polyamino acids (MW: 2500-10,000), such as polyaspartic acid (cation sorption), polyarginine (oxyanion sorption), and polycysteine (chelation exchange), directly on the membrane pore surfaces. Since these sorbents have also been found to have high selectivity over non-toxic metals, such as calcium, they are ideal candidates for hybrid processing with RO/NF. (C) 2002 Elsevier Science B.V All rights reserved.
引用
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页码:21 / 32
页数:12
相关论文
共 31 条
[1]   Removal of ions in nickel electroplating rinse water using low-pressure nanofiltration [J].
Ahn, KH ;
Song, KG ;
Cha, HY ;
Yeom, IT .
DESALINATION, 1999, 122 (01) :77-84
[2]   REMOVAL OF AMMONIUM AND NITRATE IONS FROM MINE EFFLUENTS BY MEMBRANE TECHNOLOGY [J].
AWADALLA, FT ;
STRIEZ, C ;
LAMB, K .
SEPARATION SCIENCE AND TECHNOLOGY, 1994, 29 (04) :483-495
[3]   Novel poly-glutamic acid functionalized microfiltration membranes for sorption of heavy metals at high capacity [J].
Bhattacharyya, D ;
Hestekin, JA ;
Brushaber, P ;
Cullen, L ;
Bachas, LG ;
Sikdar, SK .
JOURNAL OF MEMBRANE SCIENCE, 1998, 141 (01) :121-135
[4]  
BHATTACHARYYA D, 1998, ENCY ENV ANAL REMEDI, P4149
[5]   The application of reverse osmosis and nanofiltration to the removal of nitrates from groundwater [J].
Bohdziewicz, J ;
Bodzek, M ;
Wasik, E .
DESALINATION, 1999, 121 (02) :139-147
[6]   Nitrate removal and water quality improvements with reverse osmosis for Brighten, Colorado [J].
Cevaal, JN ;
Suratt, WB ;
Burke, JE .
DESALINATION, 1995, 103 (1-2) :101-111
[7]  
Dyer J, 1998, EARLY MUSIC HIST, V17, P1, DOI 10.1002/ep.670170112
[8]   Ultra-low pressure RO membranes: an analysis of performance and cost [J].
Filteau, G ;
Moss, P .
DESALINATION, 1997, 113 (2-3) :147-152
[9]   New membrane developments expanding the horizon for the application of reverse osmosis technology [J].
Gerard, R ;
Hachisuka, H ;
Hirose, M .
DESALINATION, 1998, 119 (1-3) :47-55
[10]   Aspects of microfiltration and reverse osmosis in municipal wastewater reuse [J].
Ghayeni, SBS ;
Madaeni, SS ;
Fane, AG ;
Schneider, RP .
DESALINATION, 1996, 106 (1-3) :25-29