Ion exchange equilibrium between cation exchange membranes and aqueous solutions of K+/Na+, K+/Ca2+, and Na+/Ca2+

被引:6
|
作者
Hannachi, Ch. [1 ]
Hamrouni, B. [2 ]
Dhahbi, M. [1 ]
机构
[1] Lab Eau & Technol Membranaires, Soliman 8020, Tunisia
[2] Fac Sci Tunis, UR Traitement & Dessalement Eaux, Manar 2092 II, Tunisia
关键词
Ion exchange membrane; Selectivity coefficient; Isotherms; Binary system; Ternary system; WASTE-WATER; ELECTRODIALYSIS;
D O I
10.1007/s11581-008-0292-2
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Equilibrium between synthetic ion exchangers and solutions of cations has been the subject of this investigation. Competitive ion exchange reactions were studied for two cation exchange membranes (CMX and CRP) involving K+, Na+, and Ca2+ ions. The ionic strength of the equilibrating solutions was maintained constant, but the molar fraction varied; all experiments were conduced with nitrate as nonexchanging anions at 25 degrees C. Adsorption isotherm for the three binaries systems: K+/Na+, K+/Ca2+, and Na+/Ca2+ were studied. The obtained results show that potassium was the most strongly sorbed and the selectivity order for CMX and CRP membranes is K+>Ca2+>Na+ at 0.1 M, under the experimental conditions. Selectivity coefficients K-K+(Na+), K-2Na+(Ca2+), and K-2K+(Ca2+) for the three binaries and for the two membranes were determined at an ionic strength of 0.1 M and at a constant temperature of 25 degrees C. We remark that all the selectivity coefficient values are quite different from the unit. Ternary equilibrium was taken for the Ca2+/K+/Na+ system. It was found that binary selectivity data could be successfully used to predict the ternary ion exchange equilibrium.
引用
收藏
页码:445 / 451
页数:7
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