Dissemin is shutting down on January 1st, 2025

Published in

Elsevier, Separation and Purification Technology, (104), p. 333-341

DOI: 10.1016/j.seppur.2012.11.033

Links

Tools

Export citation

Search in Google Scholar

A hybrid photocatalysis–ultrafiltration continuous process for humic acids degradation

Journal article published in 2013 by S. I. Patsios ORCID, V. C. Sarasidis, A. J. Karabelas
This paper is available in a repository.
This paper is available in a repository.

Full text: Download

Green circle
Preprint: archiving allowed
Red circle
Postprint: archiving forbidden
Red circle
Published version: archiving forbidden
Data provided by SHERPA/RoMEO

Abstract

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.