Removal of humic acid foulant from ultrafiltration membrane surface using photocatalytic oxidation process.
The experimental results indicated that without the TiO2 particles and PCO treatment, the permeate flux of ultrafiltration (UF) membrane declined to 40% of the initial permeate flux after 8 hours filtration. Feeding the humic acid solution with TiO2 particles dosage of 1 g/L with calcium ions into UF membrane, after the same filtration time and PCO reaction at 120 minutes, the permeate flux was increased to about 90% of the initial permeate flux. At longer PCO reaction times, a better water quality of UF permeate was observed. It has been found that with the coexistence of calcium ions in humic acid solution, the smaller molecular fragments of humic acid (HA) generated by PCO reaction may be transferred to the surface of TiO2 by means of adsorption. The humic acid adsorption by TiO2 in the presence of Ca2+ is also pH dependent. The adsorption rates were 21.0, 14.9 and 10.8 ppmTOC/gTiO2 for pH value of 4, 7 and 10 respectively. The combination of effects of PCO mineralization of humic acid into CO2 and adsorption of humic acid by TiO2 through the forming of HA-Ca(2+)-TiO2 aggregate particles were responsible for the removal of humic acid foulant from UF membrane surface.
Fang
H
H
SUT Sakra Pte Ltd, 51 Sakra Avenue, Singapore 627894.
Sun
D D
DD
Wu
M
M
Phay
W
W
Tay
J H
JH
D000327:Adsorption; D002245:Carbon Dioxide / Q000737:chemistry; D002384:Catalysis; D004868:Equipment Failure; D006812:Humic Substances; D008567:Membranes, Artificial; D010084:Oxidation-Reduction; D010539:Permeability; D010777:Photochemistry; D013997:Time Factors; D014025:Titanium / Q000494:pharmacology; D014462:Ultrafiltration; D014865:Waste Disposal, Fluid / Q000379:methods*; D018508:Water Purification / Q000379:methods*
D006812:Humic Substances; D008567:Membranes, Artificial; D002245:Carbon Dioxide; C009495:titanium dioxide; D014025:Titanium