TY - JOUR
T1 - Modeling of fluoride rejection from aqueous solution by nanofiltration process
T2 - Single and binary solution
AU - Fatehizadeh, Ali
AU - Amin, Mohammad Mehdi
AU - Sillanpää, Mika
AU - Hatami, Nahid
AU - Taheri, Ensiyeh
AU - Baghaei, Najmeh
AU - Mahajan, Shreya
N1 - Publisher Copyright:
© 2020 Desalination Publications. All rights reserved.
PY - 2020/7
Y1 - 2020/7
N2 - This study was aimed at the investigation of fluoride (F–) rejection from single and binary solution by nanofiltration process (NF). The influence of various parameters such as the effect of solution pH, initial F– concentration, applied pressure, feed flux, and accompanying cations and anions in feed water has been reported. Besides, the solute rejection and Spiegler–Kedem models were applied for the better understanding of NF performance. In a single solution, the laboratory study demonstrated F– rejections with NF membranes to be higher than 85%. Moreover, as applied pressure and feed flux increased F– rejection was observed to increase marginally whereas the opposite trend was observed when initial F– concentration in feed water was increased. Further, the depletion of F– rejection at 15 mg/L of F– was found to be associated with the presence of co-existing cation and anion in the feed water. The estimated average of pore radius and Δx/Ak of the NF membrane were 0.12 ± 0.02 nm and 47.84 ± 25.22 mm, respectively.
AB - This study was aimed at the investigation of fluoride (F–) rejection from single and binary solution by nanofiltration process (NF). The influence of various parameters such as the effect of solution pH, initial F– concentration, applied pressure, feed flux, and accompanying cations and anions in feed water has been reported. Besides, the solute rejection and Spiegler–Kedem models were applied for the better understanding of NF performance. In a single solution, the laboratory study demonstrated F– rejections with NF membranes to be higher than 85%. Moreover, as applied pressure and feed flux increased F– rejection was observed to increase marginally whereas the opposite trend was observed when initial F– concentration in feed water was increased. Further, the depletion of F– rejection at 15 mg/L of F– was found to be associated with the presence of co-existing cation and anion in the feed water. The estimated average of pore radius and Δx/Ak of the NF membrane were 0.12 ± 0.02 nm and 47.84 ± 25.22 mm, respectively.
KW - Cost evaluation
KW - Drinking water
KW - Fluoride rejection
KW - Membrane modeling
KW - Nanofiltration
UR - http://www.scopus.com/inward/record.url?scp=85098650631&partnerID=8YFLogxK
U2 - 10.5004/dwt.2020.25831
DO - 10.5004/dwt.2020.25831
M3 - Article
AN - SCOPUS:85098650631
SN - 1944-3994
VL - 193
SP - 224
EP - 234
JO - Desalination and Water Treatment
JF - Desalination and Water Treatment
ER -