Elsevier, Separation and Purification Technology, (104), p. 333-341
DOI: 10.1016/j.seppur.2012.11.033
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a b s t r a c t The successful operation of a hybrid photocatalysis–membrane separation process (in a laboratory-scale pilot system) is demonstrated for degradation of Humic Acids (HAs), which are typical refractory compo-nents of Natural Organic Matter (NOM). The Photocatalytic Membrane Reactor (PMR) employing an Ultrafiltration (UF) submerged module was operated in continuous mode with TiO 2 catalyst concentra-tion 0.75 g/L and UV-A radiant flux 15.1 J/s, treating feed water with HA concentrations 5.0 and 10.0 mg/L. Experiments carried out within a sufficiently broad pH range (approx. 3.5–7.0) exhibited sat-isfactory HA mineralization rates and rather high HA mineralization efficiencies; a near optimum pH at approx. 5.5 was identified. The overall process removal efficiency (comprising both HA oxidation and UF membrane rejection) was even higher, as a result of the synergistic effects of photocatalytic oxidation and membrane filtration. The degradation of HA aromatic rings, that diminishes the Disinfection By-Products (DBPs) formation potential, was also very high; the specific UV-A 254 removal efficiency was greater than 95% in almost all cases studied. Concerning membrane filtration performance, the periodic backwashing employed, combined with the moderate membrane flux, effectively controlled membrane fouling thus permitting stable continuous operation with no wastewater stream. Ó 2012 Elsevier B.V. All rights reserved.