Environmental and Energy Engineering
Double-deck aerated biofilm membrane bioreactor with sludge control for municipal wastewater treatment
Article first published online: 7 APR 2009
DOI: 10.1002/aic.11736
Copyright © 2009 American Institute of Chemical Engineers (AIChE)
Additional Information
How to Cite
Phattaranawik, J. and Leiknes, T. (2009), Double-deck aerated biofilm membrane bioreactor with sludge control for municipal wastewater treatment. AIChE J., 55: 1291–1297. doi: 10.1002/aic.11736
Publication History
- Issue published online: 14 APR 2009
- Article first published online: 7 APR 2009
- Manuscript Revised: 24 SEP 2008
- Manuscript Received: 27 MAR 2008
Funded by
- European Commission. Grant Number: 018480
- EUROMBRA
- European Commission under the Sixth Framework Programme (Priority “Global Change and Ecosystems”)
- AnoxKaldnes for biofilm media
- A3 Water Solutions GmbH, Germany
- Abstract
- Article
- References
- Cited By
Keywords:
- biofilm membrane bioreactor;
- bioreactor design;
- sludge control;
- moving-bed biofilm;
- flat sheet membrane modules
Abstract
Alternative designs of an aerated moving-bed biofilm reactor and a flat-sheet membrane module for a biofilm membrane bioreactor process have been investigated to overcome a membrane clogging problem and to determine the performance of a new membrane module. Double-deck aerated biofilm reactor with integrated designs of sludge hopper, thickener, and velocity-zone concept for particle settlement was evaluated for the suspended solid control and removal. Hydrodynamics of bubbling, liquid, and solid particles were arranged in the bioreactor to obtain a particle settlement. New membrane modules used under low suspended solid environment having smaller membrane gaps were evaluated for filtration performance and clogging problems for long-term operation. The average suspended solids concentration in the bioreactor effluent was 44.6 mg/L. Relaxation applied with the membrane module provided the most optimum result for fouling control, and no clogging problems in the modules were observed in the system after continuous operation of 3 weeks. © 2009 American Institute of Chemical Engineers AIChE J, 2009

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