Diffusion coefficients of ions through ion exchange membrane in Donnan dialysis using ions of different valence

被引:60
作者
Miyoshi, H [1 ]
机构
[1] Univ Osaka Prefecture, Adv Sci & Technol Res Inst, Osaka 5998570, Japan
关键词
diffusion coefficients; Donnan dialysis; ion exchange membranes;
D O I
10.1016/S0376-7388(97)00297-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Donnan dialysis with an ion exchange membrane was investigated for ions of different valence. The effective diffusion coefficients (D-e) of various kinds of ions in the membrane were obtained by fitting of the equation derived from the Nernst-Planck equation to three or more sets of experimental data for Donnan dialysis. It became apparent that the value of D-e/D-s of monovalent ions (e.g., K+ or Na+ ions) at z(A) = 1 and z(B) = 2 (feed ions are monovalent ones and driving ions are bivalent ones) remained constant at ca. 1/210 and that of bivalent ions (e.g., Ca2+, Cu2+, Or Mg2+ ions) remained constant at ca. 1/526 where D-s denotes the diffusion coefficient of ions at infinite dilution in water calculated from the Nernst-Einstein equation, and z(A) and z(B) represent the valences of the feed and driving ions, respectively. D-e/D-s of monovalent ions (e.g., H+, K+, or Na+ ions) at z(A) = 2 and z(B) = 1 (feed ions are bivalent ones and driving ions are monovalent ones) was constant at ca. 1/23.3 and that of bivalent ions remained constant at ca. 1/58.4. It was proved that D-e/D using D-e at z(A) = 1 and z(B) = 2 was constant at 1/3.0 and that at z(A) = 2 and z(B) = 1 remained constant at 3.0 where D represents the diffusion coefficient of ions in the membrane at z(A) = z(B) (the valences of both feed and driving ions are equal). Therefore, it was found that a large flux of ions could be obtained using the monovalent driving ions in Donnan dialysis. On the other hand, the small flux can be obtained using bi- or higher-valent driving ions. (C) 1998 Elsevier Science B.V.
引用
收藏
页码:101 / 110
页数:10
相关论文
共 13 条
[1]  
HELFFERICH F, 1962, ION EXCHANGE, P268
[2]  
HEN NK, 1993, KAGAKU BINRAN, V2
[3]   MEMBRANE DIFFUSION-CONTROLLED KINETICS OF IONIC TRANSPORT [J].
HO, CC ;
JAN, DS ;
TSAI, FN .
JOURNAL OF MEMBRANE SCIENCE, 1993, 81 (03) :287-294
[4]   A FUNDAMENTAL-STUDY ON RECOVERY OF COPPER WITH A CATION-EXCHANGE MEMBRANE .2. TRANSFER RATE OF COPPER AND HYDROGEN-ION THROUGH A CATION-EXCHANGE MEMBRANE [J].
KOJIMA, T ;
FURUSAKI, S ;
SAITO, K .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1982, 60 (05) :650-658
[5]  
Lakshminarayanaiah N., 1969, TRANSPORT PHENOMENA, P158
[6]   Diffusion coefficients of ions through ion-exchange membranes for Donnan dialysis using ions of the same valence [J].
Miyoshi, H .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (07) :1087-1096
[7]   CHARACTERISTIC COEFFICIENTS OF CATION-EXCHANGE MEMBRANES FOR BIVALENT-CATIONS IN EQUILIBRIUM BETWEEN THE MEMBRANE AND SOLUTION [J].
MIYOSHI, H ;
YAMAGAMI, M ;
CHUBACHI, M ;
KATAOKA, T .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1994, 39 (03) :595-598
[8]   CHARACTERISTIC COEFFICIENTS FOR EQUILIBRIUM BETWEEN SOLUTION AND NEOSEPTA OR SELEMION CATION-EXCHANGE MEMBRANES [J].
MIYOSHI, H ;
CHUBACHI, M ;
YAMAGAMI, M ;
KATAOKA, T .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1992, 37 (01) :120-124
[9]   ESTIMATION OF THE LIMITING CURRENT-DENSITY IN ELECTRODIALYSIS WITH BOTH SPACER AND SPACE [J].
MIYOSHI, H ;
KATAOKA, T .
SEPARATION SCIENCE AND TECHNOLOGY, 1989, 24 (7-8) :507-515
[10]  
MIYOSHI H, 1988, SEPAR SCI TECHNOL, V2, P585