Ion exchange resin-Bipolar membrane electrodialysis hybrid process for reverse osmosis permeate remineralization: Cation exchange resins equilibria and kinetics

被引:16
作者
Abusultan, A. A. M. [1 ]
Wood, J. A. [1 ]
Sainio, T. [2 ]
Kemperman, A. J. B. [1 ]
van der Meer, W. G. J. [1 ,3 ]
机构
[1] Univ Twente, MESA Inst Nanotechnol, Fac Sci & Technol, Membrane Sci & Technol Cluster, POB 217, NL-7500 AE Enschede, Netherlands
[2] LUT Univ, Sch Engn Sci, Dept Separat Sci, Mukkulankatu 19, Lahti 15210, Finland
[3] Oasen NV, POB 122, NL-2800 AC Gouda, Netherlands
关键词
Ion exchange resin; Sorption equilibria; Mass transfer; Chelating resin; DRINKING-WATER; MORTALITY; DESALINATION; ADSORPTION; CHEMISTRY; HARDNESS; DISEASE; MODEL;
D O I
10.1016/j.seppur.2023.123798
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Reverse osmosis (RO) membrane technology is widely used for producing high-quality drinking water. Yet RO permeate is by itself acidic (pH = 5.5 to 6.0), unbuffered and has low mineral content, therefore post treatment i. e., remineralization is mostly required. An ion exchange resin - bipolar membrane electrodialysis hybrid process was developed for sustainable RO permeate remineralization. Fundamental phenomena in the recovery of cal-cium and magnesium by ion exchange to remineralize reverse osmosis permeate were investigated. Sorption equilibrium and mass transfer kinetics were investigated for weakly acidic (Amberlite IRC747, Amberlite IRC748, Lewatit S8227) and strongly acidic (DOWEX Marathon MSC) cation exchange resins. Most suitable resin for the remineralization process should have high selectivity for calcium and magnesium and low selectivity for monovalent ions to avoid adding undesired ions to the remineralised water downstream as well as relatively fast mass transfer kinetics. The isotherms were correlated with the stoichiometric ion exchange isotherm and the Langmuir-Freundlich (Sips) isotherm. All resins showed high selectivity for ions with higher valence, but weakly acidic cation exchange (WAC) resins showed significantly lower selectivity towards monovalent ions than the strongly acidic cation exchange resin. The influence of each resin functional group, charge density and degree of protonation was shown to have a major effect on the resin selectivity. Amberlite IRC748 had the lowest selec-tivity (KNH4+/Na+ = 0.77 +/- 0.19) and removal (46%) for ammonium in a single-component system. The mass transfer rate was found to be controlled by intraparticle diffusion rather than film diffusion. Amberlite IRC748 is recommended for use in a remineralization process where divalent ions are present because of its favourable sorption and higher mass transfer kinetics (Ks = 8.65 +/- 0.58 x 10-12, 7.95 +/- 0.38 x 10-12 m2/s for calcium and magnesium, respectively).
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页数:12
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共 60 条
[1]   Stronger Bronsted Acids: Recent Progress [J].
Akiyama, Takahiko ;
Mori, Keiji .
CHEMICAL REVIEWS, 2015, 115 (17) :9277-9306
[2]  
ALLWRIGHT SP, 1974, LANCET, V2, P860
[3]   Fundamental chemistry and engineering aspects of post-treatment processes for desalinated water - A review [J].
Birnhack, Liat ;
Voutchkov, Nikolay ;
Lahav, Ori .
DESALINATION, 2011, 273 (01) :6-22
[4]   Generation of peptide maps by capillary zone electrophoresis in isoelectric iminodiacetic acid [J].
Bossi, A ;
Righetti, PG .
ELECTROPHORESIS, 1997, 18 (11) :2012-2018
[5]  
Conway B.E., 1981, Ionic Hydration in Chemistry and Biophysics
[6]  
Cotruvo J., 2009, CALCIUM MAGNESIUM DR
[7]   Heavy metals adsorption on some iminodiacetate chelating resins as a function of the adsorption parameters [J].
Dinu, Maria Valentina ;
Dragan, Ecaterina Stela .
REACTIVE & FUNCTIONAL POLYMERS, 2008, 68 (09) :1346-1354
[8]  
Drinkwaterbesluit, US
[9]   AQUEOUS AMMONIA EQUILIBRIUM CALCULATIONS - EFFECT OF PH AND TEMPERATURE [J].
EMERSON, K ;
RUSSO, RC ;
LUND, RE ;
THURSTON, RV .
JOURNAL OF THE FISHERIES RESEARCH BOARD OF CANADA, 1975, 32 (12) :2379-2383
[10]   Spatial analysis of the relationship between mortality from cardiovascular and cerebrovascular disease and drinking water hardness [J].
Ferrándiz, J ;
Abellán, JJ ;
Gómez-Rubio, V ;
López-Quilez, A ;
Sanmartín, P ;
Abellán, C ;
Martínez-Beneito, MA ;
Melchor, I ;
Vanaclocha, H ;
Zurriaga, O ;
Ballester, F ;
Gil, JM ;
Pérez-Hoyos, S ;
Ocaña, R .
ENVIRONMENTAL HEALTH PERSPECTIVES, 2004, 112 (09) :1037-1044