The kinetic transport behaviors in near interface of the membranes were studied using commercial anion and cation exchange membrane and charge mosaic membrane. Current-voltage curve gave the limiting current density that indicates the ceiling of conventional flux. From chronopotentiometry above the limiting current density, the transition time was estimated. The thickness of boundary layer was derived with conjunction with the conventional limiting current density and the transition time from steady state flux. On the other hand, the charge mosaic membrane was introduced in order to examine the ion transport on the membrane surface in detail. The concentration profile was discussed by the kinetic transport number with regard to the water dissociation (splitting) on the membrane surface. 1. Introduction It is well known that electrodialysis using ion exchange membrane makes drinking water or table salt from sea water.In Japan especially it is popular to use this electrodialysis in various fields such as food, medical pharmacy and ultrapure water [1–3]. However, the more efficient and improved electrodialysis have been required for pure water production because conventional system costs much of electric power at present. One of the main problems originates from the limiting current density that restricts the direct current for supplying through the system and depends on the thickness of diffusion layers. In this study, the way to see the thickness of the depleted solution layer was examined in order to improve the efficiency on the electrodialysis from fundamental standpoint. As mentioned above, the aim will be focused on the ionic behavior of ion transport from bulk solution to membrane surface. In addition, so far developed charge mosaic membrane [4–6] is introduced into electrodialysis model system and the ion transport mechanism is investigated. As experimental strategies, electrical methods were mainly adopted, and 4 kinds of membrane systems were selected to study: cation exchange membrane system (CMV), anion exchange membrane system (AMV), charge mosaic membrane and cation exchange membrane system (MM?+?CMV), and anion exchange membrane and charge mosaic membrane system (AMV?+?MM). The potentiometry was also used on the same membrane systems to elucidate the diffusion layer. The chronopotentiometry has been carried out to obtain the transition time [7–9]. The technique was adopted for 4 membrane arrangements to examine the contribution to the boundary layer of the charge mosaic membrane. The kinetic parameter about the boundary layer was noticed
References
[1]
T. Sata, “Ion exchange membrane,” in Royal Society of Chemistry, pp. 215–240, London, UK, 2004.
[2]
Y. Tanaka, Ion Exchange Membrane: Fundamentals and Applications, vol. 12 of Membrane Science and Technology, Elsevier, Amsterdam, The Netherlands, 2007.
[3]
T. Hamano, P. B. Chebi, L. Gerdes, and T. D. Wolfe, “The development of a new electrodialysis system for brackish water,” Desalination, vol. 96, pp. 23–31, 1994.
[4]
A. Yamauchi, J. Tateyama, B. I. Etoh, M. Takizawa, Y. Sugito, and S. Doi, “Charged mosaic membrane prepared from microsphere gel and its characterization,” Journal of Membrane Science, vol. 173, no. 2, pp. 275–280, 2000.
[5]
M. Takizawa, Y. Sugito, N. Oguma, M. Nakamura, S. Horiguchi, and T. Fukutomi, “Charge-mosaic membrane prepared from microspheres,” Journal of Polymer Science A, vol. 41, no. 9, pp. 1251–1261, 2003.
[6]
D. L. Grzenia, A. Yamauchi, and S. R. Wickramasinghe, “Electrolyte dialysis using charge-mosaic membranes,” Desalination and Water Treatment, vol. 4, pp. 306–310, 2009.
[7]
N. Pismenskaia, P. Sistat, P. Huguet, V. Nikonenko, and G. Pourcelly, “Chronopotentiometry applied to the study of ion transfer through anion exchange membranes,” Journal of Membrane Science, vol. 228, no. 1, pp. 65–76, 2004.
[8]
J. J. Krol, M. Wessling, and H. Strathmann, “Concentration polarization with monopolar ion exchange membranes: current-voltage curves and water dissociation,” Journal of Membrane Science, vol. 162, no. 1-2, pp. 145–154, 1999.
[9]
J. J. Krol, M. Wessling, and H. Strathmann, “Chronopotentiometry and overlimiting ion transport through monopolar ion exchange membranes,” Journal of Membrane Science, vol. 162, no. 1-2, pp. 155–164, 1999.
[10]
P. Sistat and G. Pourcelly, “Chronopotentiometric response of an ion-exchange membrane in the underlimiting current-range. Transport phenomena within the diffusion layers,” Journal of Membrane Science, vol. 123, no. 1, pp. 121–131, 1997.
[11]
R. Ibanez, D. F. Stamatialis, and M. Wessling, “Role of membrane surface in concentration polarization at cation exchange membranes,” Journal of Membrane Science, vol. 239, no. 1, pp. 119–128, 2004.
[12]
A. J. Bard and L. R. Faulkner, Electrochemical Methods, Fundamentals and Applications, Wiley International Edition, 1980.
[13]
A. Yamauchi, A. M. E. Sayed, K. Mizuguchi, M. Kodama, and Y. Sugito, “Ion transport behavior in diffusion layer of new designed ion exchange-mosaic composite polymer membrane,” Journal of Membrane Science, vol. 283, no. 1-2, pp. 301–309, 2006.
[14]
T. Yawataya, Ion Exchange Membrane For Engineer, Kyoritsu Shuppan, 1982.