
Water Science & Technology Vol 41 No 10-11 pp 345353 © IWA Publishing 2000
Understanding membrane fouling in ultrafiltration of WWTP-effluent
JH Roorda* and JH van der Graaf**
*
Department of Sanitary Engineering, Faculty of Civil Engineering and Geosciences, Delft University of Technology, P.O. BOX 5048, NL-2600 GA Delft, The Netherlands. (E-mail: J.Roorda@CiTG.TUDelft.nl)
**
Department of Sanitary Engineering, Faculty of Civil Engineering and Geosciences, Delft University of Technology, P.O. BOX 5048, NL-2600 GA Delft, The Netherlands. (E-mail: J.Roorda@CiTG.TUDelft.nl)
ABSTRACT
The application of ultrafiltration to effluent of waste water treatment
plants (WWTP-effluent) is getting increasing attention. However, many
experiments show a rapid decrease in flux urging frequent and intensive
cleaning. In order to understand the mechanisms of the occurring fouling
process, various filtration and cleaning experiments were performed, giving
information about the filterability of the feedwater (F) and the
reversibility of the occurring fouling layer (R). Short-term fluxes are
mainly determined by the filterability, while both the filterability and
the reversibility greatly affect long-term fluxes. The objective of this
research is to measure the filterability of WWTP-effluent and the
reversibility of the occurring fouling layer in ultrafiltration of
wwtp-effluent with and without pre-treatment.
The results of the filtration experiments show a rapid decrease of flux
resulting in a low value for the filterability, which also decreases during
progressing filtration. The filterability is mainly related to the volume of
treated water. Pre-treatment of the WWTP-effluent by in-line coagulation or
by deep-bed filtration has little influence on the filterability. However,
results on the reversibility show an improvement of the reversibility by
pre-treatment. Both filterability of the WWTP-effluent and reversibility of
the fouling layer are found to be independent of the applied flux.
As to the applied cleaning methods, the back flush is far more effective
than the forward flush even if combined with air. In all experiments the
remaining fouling layer still has to be removed by an intensive chemical
cleaning. This research indicates the very importance of reducing the
formation of an irreversible, non-removable fouling layer.
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