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Received May 3, 2009
Accepted September 21, 2009
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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A study on submerged rotating MBR for wastewater treatment and membrane cleaning

Key Lab for Green Processing and Functional Textile of New Textile Materials (Ministry of Education), Wuhan University of Science and Engineering, Wuhan, 430073, P. R. China 1Department of Industrial Engineering, Wuhan University of Science and Engineering, Wuhan, 430073, P. R. China 2Key Laboratory for Catalysis and Material Science of Hubei Province, South-Central University for Nationalities, Wuhan, 430074, P. R. China
Korean Journal of Chemical Engineering, March 2010, 27(3), 881-885(5), 10.1007/s11814-010-0123-9
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Abstract

A submerged rotating membrane bioreactor (SRMBR), with a rotatable, rounded, flat-sheet Poly(vinyldiene fluoride) (PVDF) membrane module fixed on hollow axes and moved by an electromotor, was used for wastewater reclamation. It was found that the effluent COD became stable and lower than 20 mg/L after one day running. The equilibrium permeate flux increased from 42.5 to 47.5 L/m2·h with the rotation speed increasing from 15 r/min to 25 r/min. Prolonging relaxation time could alleviate membrane fouling and enhance the flux. Finally, membrane cleaning was studied. The results showed that flushing the membrane surface with water, water/NaOH and water/NaOH/HCl recovered permeate flux to 48.4%, 83.5% and 90.2% of that of the initial operation, respectively.

References

Lee W, Kang S, Shin H, J. Membr. Sci., 216(1-2), 217 (2003)
Hai FI, Yamamoto K, Fukushi K, Desalination, 180(1-3), 89 (2005)
Cicek N, Winna H, Suidan MT, Wrenn BE, Urbain V, Manem J, Water Res., 32, 1553 (1998)
Jung CW, Kang LS, Korean J. Chem. Eng., 20(5), 855 (2003)
Thiruvenkatachari R, Shim WG, Lee JW, Moon H, Korean J. Chem. Eng., 22(2), 250 (2005)
Phattaranawik J, Fane AG, Pasquier ACS, Bing W, Desalination, 223(1-3), 386 (2008)
Yu HY, Xu ZK, Xie YJ, Liu ZM, Wang SY, J. Membr. Sci., 279(1-2), 148 (2006)
Howell JA, Chua HC, Arnot TC, J. Membr. Sci., 242(1-2), 13 (2004)
Le-Clech P, Jefferson B, Judd SJ, Desalination, 173(2), 113 (2005)

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