Effects of Aeration Intensity on Membrane Fouling in A Membrane Bioreactor Treating Domestic Wastewater

Date Received: 05-06-2025

Date Published: 13-06-2025

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TÀI NGUYÊN VÀ MÔI TRƯỜNG

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Uan, D., & Yeom, I. (2025). Effects of Aeration Intensity on Membrane Fouling in A Membrane Bioreactor Treating Domestic Wastewater. Vietnam Journal of Agricultural Sciences, 10(1). https://doi.org/10.31817/tckhnnvn.2012.10.1.

Effects of Aeration Intensity on Membrane Fouling in A Membrane Bioreactor Treating Domestic Wastewater

Do Khac Uan (*) , Ick T. Yeom

  • Tác giả liên hệ: [email protected]
  • Keywords

    Aeration intensity, cross flow velocity, membrane fouling, wastewater

    Abstract


     

    Membrane fouling is one of the great challenges for application of membrane bioreactor technology to wastewater treatment. Aeration system is a key factor to avoid the sludge cumulated on the membrane surface. The effects of aeration intensity on the cross flow velocity and membrane fouling were determined in this study. As a result, the cross flow velocity was increased with increasing in aeration intensity. When aeration intensity was increased from 0.014 to 0.069 L/cm2/min, the cross flow velocity was increased rapidly. However, it was almost unchanged when aeration intensity was higher than 0.069 L/cm2/min. The transmembrane pressure was also increased quickly when the cross flow velocity was lower than the critical velocity (30.5 cm/s). When the cross flow velocity was higher than 30.5 cm/s, the transmembrane pressure was increased negligible. Therefore, the air flowrate should be controlled to make sure the cross flow velocity to be higher than the critical value. This will prevent the membrane fouling and help the system to be operated longer.

    References

    Banu, R., D.K. Uan, I.J. Chung & I.T. Yeom (2009). A study on nutrient removal and membrane performance in A2O-MBR treating domestic wastewater. J. Env. Bio., 30: 959-963.

    Cornel, P. & S. Krause (2006). Membrane bioreactors in industrial wastewater treatment - European experiences, examples and trends. Water Sci. Tech., 53: 37-44.

    Choi, J.H., K. Fukushi & K. Yamamoto (2007). A submerged nanofiltration membrane bioreactor for domestic wastewater treatment: the performance of cellulose acetate nanofiltration membranes for long-term operation. Sep. Purif. Tech., 52: 470-477.

    Lobos, J., C. Wisniewski, M. Heran & A. Grasmick (2006). Membrane bioreactor performances: comparison between continuous and sequencing systems. Desalination, 199: 319-321.

    Melin, T., B. Jefferson, D. Bixio, C. Thoeye, W. De Wilde, J. De Koning, J. van der Graaf & T. Wintgens (2006). Membrane bioreactor technology for wastewater treatment and reuse. Desalination, 187: 271-282.

    Qin, J.J., M. N. Wai, G. Tao, K.A. Kekre & H. Seah (2007). Membrane bioreactor study for reclamation of mixed sewage mostly from industrial sources. Sep. Purif. Tech., 53: 296-300.

    Rosenberger, S., U. Krüger, R. Witzig, W. Manz, U. Szewzyk & M. Kraume (2002). Performance of a bioreactor with submerged membranes for aerobic treatment of municipal waste water. Water Res., 36: 413-420.

    Trouve, E., V. Urbain & J. Manem (1994). Treatment of municipal wastewater by a membrane bioreactor: Results of a semi-industrial pilot-scale study. Water Sci. Tech., 30: 151-157.

    Uan, D.K. & D.K. Chi (2008). An assessment of potential application of membrance technology in municipal wastewater treatment in Vietnam. J. Urban Env., 7: 39-42.

    Uan, D.K., R. Banu, S. Kaliappan & I.T. Yeom (2009). Application of membrane filtration to organic and nutrient removal in municipal wastewater using anaerobic-anoxic-aerobic bioreactor. Vietnam National Conference on Biological Technology. Thai Nguyen University & Institute of BioTechnology, 26-27 Nov. 2009, pp. 950-953.

    van der Graaf, J.H., J.F. Kramer, J. Pluim, J. de Koning & M. Weijs (1999). Experiments on membrane filtration of effluent at wastewater treatment plants in Netherlands. Water Sci. Tech., 39: 129-136.