TY - JOUR
T1 - Transport characteristics of neutralization dialysis and desalination of tap water
AU - Igawa, Manabu
AU - Mikami, Kentaro
AU - Okochi, Hiroshi
PY - 2003
Y1 - 2003
N2 - In neutralization dialysis, the salt solution is desalinated continuously. The cations in desalination compartment are exchanged with protons in the acid compartment across a cation-exchange membrane and the anions are exchanged with hydroxide ions in the base compartment across an anion-exchange membrane. A simple index (C/J), where C is the source phase concentration (mol cm-3) and J is the flux (mol cm-2 min-1), was proposed for the estimation of the desalination properties in neutralization dialysis. The index was based on the concepts of the ion-exchange reaction rate at the membrane interface and was related to the permeation constant in the source-phase boundary layer at the membrane interface, Pa (cm min-1), as C/J = 1/(k1·Cex) + 1/Pa, where k1 is the rate constant of ion-exchange reaction (mol-1 cm4 min-1) and Cex is the ion exchange capacity of the membrane (mol cm-3). The desalination efficiency increased with the decrease of the desalination compartment thickness and the decrease of the linear velocity, which can be estimated well by using the index. Tap water was desalinated by neutralization dialysis and pure water was obtained at the outlet of the desalination cell.
AB - In neutralization dialysis, the salt solution is desalinated continuously. The cations in desalination compartment are exchanged with protons in the acid compartment across a cation-exchange membrane and the anions are exchanged with hydroxide ions in the base compartment across an anion-exchange membrane. A simple index (C/J), where C is the source phase concentration (mol cm-3) and J is the flux (mol cm-2 min-1), was proposed for the estimation of the desalination properties in neutralization dialysis. The index was based on the concepts of the ion-exchange reaction rate at the membrane interface and was related to the permeation constant in the source-phase boundary layer at the membrane interface, Pa (cm min-1), as C/J = 1/(k1·Cex) + 1/Pa, where k1 is the rate constant of ion-exchange reaction (mol-1 cm4 min-1) and Cex is the ion exchange capacity of the membrane (mol cm-3). The desalination efficiency increased with the decrease of the desalination compartment thickness and the decrease of the linear velocity, which can be estimated well by using the index. Tap water was desalinated by neutralization dialysis and pure water was obtained at the outlet of the desalination cell.
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U2 - 10.1246/bcsj.76.437
DO - 10.1246/bcsj.76.437
M3 - Article
AN - SCOPUS:0037249008
SN - 0009-2673
VL - 76
SP - 437
EP - 441
JO - Bulletin of the Chemical Society of Japan
JF - Bulletin of the Chemical Society of Japan
IS - 2
ER -