TY - JOUR
T1 - Removal of chloride from ethylene glycol solution using alumina/zeolite membrane as a physical boundary between the organic and aqueous phases
AU - Kameda, Tomohito
AU - Shoji, Chisato
AU - Fukushima, Shoko
AU - Grause, Guido
AU - Yoshioka, Toshiaki
PY - 2013/9
Y1 - 2013/9
N2 - The permeation of Cl- ions from a NaCl/ethylene glycol (EG) solution during electrodialysis was investigated using alumina and alumina/zeolite membranes. Voltage changes had very little effect on Cl- permeation through the alumina membrane, suggesting that the driving force for the permeation was concentration-gradient-induced diffusion, and not the electric field. Solvation of the Na+ ions by EG resulted in EG migration through the membrane. Replacement of the deionized water (electrolyte) in the anodic cell with NaOH resulted in increased Cl- permeation, although a greater amount of EG migrated into the NaOH solution as well. No notable difference was observed in Cl- permeation through the alumina and alumina/zeolite membranes, but EG migration decreased when using the latter membrane, suggesting that EG migration was prevented by the zeolite layer. The proposed alumina/zeolite membrane is, hence, useful for solvent recovery by electrodialysis, but its mechanical stability must be improved for industrial applications.
AB - The permeation of Cl- ions from a NaCl/ethylene glycol (EG) solution during electrodialysis was investigated using alumina and alumina/zeolite membranes. Voltage changes had very little effect on Cl- permeation through the alumina membrane, suggesting that the driving force for the permeation was concentration-gradient-induced diffusion, and not the electric field. Solvation of the Na+ ions by EG resulted in EG migration through the membrane. Replacement of the deionized water (electrolyte) in the anodic cell with NaOH resulted in increased Cl- permeation, although a greater amount of EG migrated into the NaOH solution as well. No notable difference was observed in Cl- permeation through the alumina and alumina/zeolite membranes, but EG migration decreased when using the latter membrane, suggesting that EG migration was prevented by the zeolite layer. The proposed alumina/zeolite membrane is, hence, useful for solvent recovery by electrodialysis, but its mechanical stability must be improved for industrial applications.
KW - Alumina membrane
KW - Alumina/zeolite membrane
KW - Chloride
KW - Electrodialysis
KW - Ion permeation
UR - http://www.scopus.com/inward/record.url?scp=84883653015&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=84883653015&partnerID=8YFLogxK
U2 - 10.1007/s10163-013-0119-8
DO - 10.1007/s10163-013-0119-8
M3 - Comment/debate
AN - SCOPUS:84883653015
SN - 1438-4957
VL - 15
SP - 404
EP - 408
JO - Journal of Material Cycles and Waste Management
JF - Journal of Material Cycles and Waste Management
IS - 3
ER -