The potential of membrane bioreactor (MBR) systems to remove organic micropollutants was investigated at different scales, operational conditions, and locations. The effluent quality of the MBR system was compared with that of a plant combining conventional activated sludge (CAS) followed by ultrafiltration (UF). The MBR and CAS-UF systems were operated and tested in parallel. An MBR pilot plant in Israel was operated for over a year at a mixed liquor suspended solids (MLSS) range of 2.8–10.6 g/L. The MBR achieved removal rates comparable to those of a CAS-UF plant at the Tel-Aviv wastewater treatment plant (WWTP) for macrolide antibiotics such as roxythromycin, clarithromycin, and erythromycin and slightly higher removal rates than the CAS-UF for sulfonamides. A laboratory scale MBR unit in Berlin – at an MLSS of 6–9 g/L – showed better removal rates for macrolide antibiotics, trimethoprim, and 5-tolyltriazole compared to the CAS process of the Ruhleben sewage treatment plant (STP) in Berlin when both were fed with identical quality raw wastewater. The Berlin CAS exhibited significantly better benzotriazole removal and slightly better sulfamethoxazole and 4-tolyltriazole removal than its MBR counterpart. Pilot MBR tests (MLSS of 12 g/L) in Aachen, Germany, showed that operating flux significantly affected the resulting membrane fouling rate, but the removal rates of dissolved organic matter and of bisphenol A were not affected.
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Research Article|
February 01 2011
Comparison of two treatments for the removal of selected organic micropollutants and bulk organic matter: conventional activated sludge followed by ultrafiltration versus membrane bioreactor
E. Sahar;
1Ben-Gurion University, P.O. B 653, 84105 Beer-Sheva, Israel E-mail: [email protected][email protected]
E-mail: [email protected]
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M. Ernst;
M. Ernst
2TU Berlin, KF4, Str. d. 17. Juni 135, 10623 Berlin, Germany E-mail: Mathias.Ernst@tu_berlin.de
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M. Godehardt;
M. Godehardt
2TU Berlin, KF4, Str. d. 17. Juni 135, 10623 Berlin, Germany E-mail: Mathias.Ernst@tu_berlin.de
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A. Hein;
A. Hein
2TU Berlin, KF4, Str. d. 17. Juni 135, 10623 Berlin, Germany E-mail: Mathias.Ernst@tu_berlin.de
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J. Herr;
J. Herr
3RWTH Aachen, Turmstr. 46, 52056 Aachen, Germany E-mail: [email protected]
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C. Kazner;
C. Kazner
3RWTH Aachen, Turmstr. 46, 52056 Aachen, Germany E-mail: [email protected]
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T. Melin;
T. Melin
3RWTH Aachen, Turmstr. 46, 52056 Aachen, Germany E-mail: [email protected]
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H. Cikurel;
H. Cikurel
4Mekorot, 9 Lincoln Street, 61201 Tel-Aviv, Israel E-mail: [email protected]
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A. Aharoni;
A. Aharoni
4Mekorot, 9 Lincoln Street, 61201 Tel-Aviv, Israel E-mail: [email protected]
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R. Messalem;
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R. Messalem
1Ben-Gurion University, P.O. B 653, 84105 Beer-Sheva, Israel E-mail: [email protected][email protected]
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A. Brenner;
A. Brenner
1Ben-Gurion University, P.O. B 653, 84105 Beer-Sheva, Israel E-mail: [email protected][email protected]
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M. Jekel
M. Jekel
2TU Berlin, KF4, Str. d. 17. Juni 135, 10623 Berlin, Germany E-mail: Mathias.Ernst@tu_berlin.de
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Water Sci Technol (2011) 63 (4): 733–740.
Citation
E. Sahar, M. Ernst, M. Godehardt, A. Hein, J. Herr, C. Kazner, T. Melin, H. Cikurel, A. Aharoni, R. Messalem, A. Brenner, M. Jekel; Comparison of two treatments for the removal of selected organic micropollutants and bulk organic matter: conventional activated sludge followed by ultrafiltration versus membrane bioreactor. Water Sci Technol 1 February 2011; 63 (4): 733–740. doi: https://doi.org/10.2166/wst.2011.300
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