Modeling of biofouling by extracellular polymers in a membrane separation activated sludge system

A Laboratory-scale experiment was conducted to investigate the mechanism of the bio-fouling in the submerged membrane separation activated sludge syst em. Flat-sheet-type membrane module was used and the change of the pressure and the filtration resistance was measured. Two reactors were operated in parallel to investigate the influence of organic loading rate on the reacto r performance. A mathematical model was developed to simulate temporal chan ges of suction pressure, flux and filtration resistance considering accumul ation, detachment and consolidation of EPS on the membrane surface. Paramet ers in the model were determined so that the calculated results fit to the measured variation curves. The high load reactor (1.5g-TOC L-1 day(-1)) sho wed a sudden increase of the pressure and a decrease of flux after 40(th) d ays, which could not be recovered even by membrane cleanings, while the low load reactor(0.5g-TOC L-1 day(-1)) showed little increase of the pressure until 120th days. The measured pattern of the flux, the pressure and the re sistance were well explained by the developed model. Using the model, influ ence of operational parameters, such as organic loading rate, flux and shea r stress working on the membrane, on the reactor performance was evaluated. It was concluded that the flux is the most influential parameter and when the flux is more than a critical value, which is as low as 0.1 m day(-1), m aximum time during which the set flux can be maintained becomes very short. (C) 1998 Published by Elsevier Science Ltd. All rights reserved.