Effect of HIx solution concentration on ion-exchange membrane performance in electro-electrodialysis
Tanaka, Nobuyuki
; Yamaki, Tetsuya*; Asano, Masaharu*; Terai, Takayuki*
Electro-electrodialysis (EED) has been applied to thermochemical water-splitting iodine-sulfur process for hydrogen production in order to enhance the HI component in the HI-I
-H
O mixture (HIx solution). In this paper, HIx solution concentration dependence of the conductivity (
) and transport number (
) as the membrane-performance indexes of Nafion 212 and a styrene-grafted poly(ethylene-co-tetrafluoroethylene) (ETFE) membrane was experimentally investigated. From the theoretical analysis for the measurements based on the new EED model, the effects of the H
and I
content and the diffusion coefficients of H
and I
in the evaluated membranes on
and
were as follows: HIx solution concentration dependence of ion contents exhibited a significantly small or different variation in comparison with that of
and t
, which indicates that the dominant factors for
and
would not be ion contents; thereby, the effect of ion diffusion coefficients should not be ruled out. For
of Nafion 212, H
diffusion is the dominant factor because the existence of I
was negligible, whereas for the ETFE-St membrane, the effect of I
diffusion should be considered. I
diffusion could more strongly affect
for the evaluated membranes rather than H
diffusion, which indicates that H
selectivity of the membranes could be relatively determined by the variation of the I
behavior in the membranes.