TY - JOUR
T1 - Application of nanofiltration and reverse osmosis membranes to the salty and polluted surface water
AU - Koyuncu, I.
AU - Yazgan, M.
PY - 2001
Y1 - 2001
N2 - Nanofiltration (NF) (TFC-S) and reverse osmosis (RO) (TFC-HR) membranes were evaluated for the treatment of salty and polluted Kucukcekmece Lake used as a drinking water reservoir for the Istanbul City. A thin film composite type of spiral wound membrane (2 m2 area) was used. Experiments were conducted at different pressures, pH ranges and temperatures. Flowrate was about 300 l/h. The flux decreased with increasing pH. Highest rejections were obtained for all anionic and cationic ions in the pH range of 6.0-8.5. Several permeation runs were carried out for the pressure range of 6-12 bar for TFC-S and TFC-HR membranes. According to the Spiegler-Kedem model, the permeate flux (Jv) is linearly related to the applied hydraulic pressure (ΔP). Lp values were calculated by linear regression. Salt rejection was seen to increase with the increasing of operating pressure due to increase of solvent flux. Na+, Mg+2, Ca+2, Cl- and SO4-2 rejections and Z1 and z2 constants have been determined and z values of cations were in the order of zMg > ZCa > ZNa and similarly those of anions were in the order of ZSO4 > ZCl. The Spiegle-Kedem model was able to correlate well the experimental data by fitting different best values of P and σ, respectively for all ions. Best fit values of P and σ were obtained by regression of the data according to the model.
AB - Nanofiltration (NF) (TFC-S) and reverse osmosis (RO) (TFC-HR) membranes were evaluated for the treatment of salty and polluted Kucukcekmece Lake used as a drinking water reservoir for the Istanbul City. A thin film composite type of spiral wound membrane (2 m2 area) was used. Experiments were conducted at different pressures, pH ranges and temperatures. Flowrate was about 300 l/h. The flux decreased with increasing pH. Highest rejections were obtained for all anionic and cationic ions in the pH range of 6.0-8.5. Several permeation runs were carried out for the pressure range of 6-12 bar for TFC-S and TFC-HR membranes. According to the Spiegler-Kedem model, the permeate flux (Jv) is linearly related to the applied hydraulic pressure (ΔP). Lp values were calculated by linear regression. Salt rejection was seen to increase with the increasing of operating pressure due to increase of solvent flux. Na+, Mg+2, Ca+2, Cl- and SO4-2 rejections and Z1 and z2 constants have been determined and z values of cations were in the order of zMg > ZCa > ZNa and similarly those of anions were in the order of ZSO4 > ZCl. The Spiegle-Kedem model was able to correlate well the experimental data by fitting different best values of P and σ, respectively for all ions. Best fit values of P and σ were obtained by regression of the data according to the model.
KW - Anionic and cationic pollutants
KW - Nanofiltration
KW - Reverse osmosis
KW - Salt retention
KW - Spiegler-Kedem model
UR - http://www.scopus.com/inward/record.url?scp=0034834663&partnerID=8YFLogxK
U2 - 10.1081/ESE-100104881
DO - 10.1081/ESE-100104881
M3 - Article
C2 - 11545356
AN - SCOPUS:0034834663
SN - 1093-4529
VL - 36
SP - 1321
EP - 1333
JO - Journal of Environmental Science and Health - Part A Toxic/Hazardous Substances and Environmental Engineering
JF - Journal of Environmental Science and Health - Part A Toxic/Hazardous Substances and Environmental Engineering
IS - 7
ER -