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Received September 28, 2007
Accepted November 26, 2007
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Characteristics of nitrogen and phosphorus removal in SBR and SBBR with different ammonium loading rates
Department of Environ. Sci., Catholic University of Daegu, Gyeongbuk 712-702, Korea 1Department of Health & Environment, Daegu University, Gyeongbuk 712-741, Korea
Korean Journal of Chemical Engineering, July 2008, 25(4), 793-800(8), 10.1007/s11814-008-0130-2
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Abstract
Laboratory scale experiments were conducted to study the deterioration of enhanced biological phosphorus removal (EBPR) due to influent ammonium concentration, and to compare the performance of two types of sequencing batch reactor (SBR) systems, a conventional SBR and sequencing batch biofilm reactor (SBBR). Both in SBR and SBBR, the total nitrogen removal efficiency decreased from 100% to 53% and from 87.5% to 54.4%, respectively, with the increase of influent ammonium concentration from 20 mg/l to 80 mg/l. When the influent ammonium concentration was as low as 20 mg/l (C : N : P=200 : 20 : 15), denitrifying glycogen-accumulating organisms (DGAOs) were successfully grown and activated by using glucose as a sole carbon source in a lab-scale anaerobic-oxic-anoxic (A2O) SBR. In the SBR, due to the effect of incomplete denitrification and pH drop, the nitrogen and phosphorus removal efficiency decreased from 77% to 33.3% when the influent ammonium concentration increased from 20 mg/l to 80 mg/l. However, in the SBBR, simultaneous nitrification/denitrification (SND) occurred, and the nitrification rate in the aerobic phase did not change remarkably in spite of the increase in influent ammonium concentration. Phosphorus removal was not affected by the increase of influent ammonium concentration.
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References
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Gapes D, Keller J, Biotechnol. Bioeng., 76(4), 361 (2001)
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Irvine RL, Ketchum LH, Crit. Rev. Envir. Engrg., 18, 255 (1988)
Poo KM, Im JH, Ko JH, Kim YJ, Woo HJ, Kim CW, Korean J. Chem. Eng., 22(5), 666 (2005)
Wilderer PA, Sequencing batch biofilm reactor technology. In: Harnessing biotechnology for the 21st century, Ladish M. R. and Bose A. Eds., American Chemical Society (1992)
White DM, Pilon TA, Woolard C, Water Res., 34(7), 2105 (2000)
Zhang Z, Zhou J, Wang J, Guo H, Tong J, Process Biochem., 41, 599 (2006)
Gieseke A, Arnz P, Amann R, Schramm A, Water Res., 36, 501 (2002)
Falkentoft CM, Arnz P, Henze M, Mosbaek H, Muller E, Wilderer PA, Harremoes P, Biotechnol. Bioeng., 76(1), 77 (2001)
Morgenroth E, Wilderer PA, Water Sci. Technol., 39(7), 33 (1999)
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Kuba T, van Loosdrecht MCM, Brandse FA, Heijnen JJ, Water Res., 31, 777 (1997)
Ahn J, Daidou T, Tsuneda S, Hirata A, Water Res., 36, 403 (2002)
Zeng RJ, Yuan ZG, Keller J, Biotechnol. Bioeng., 81(4), 397 (2003)
Oehmen A, Saunder A, Blackall LL, Yuan Z, Keller J, Presented at the IWA world water congress, Melbourne, Australia (2002)
Munch EV, Lant PA, Keller J, Water Res., 30(2), 277 (1996)
Guo H, Zhou J, Su J, Zhang Z, Biochem. Eng. J., 23, 57 (2005)
Zeng RJ, Lemaire R, Yuan Z, Keller J, Water Sci. Technol., 50(10), 163 (2004)
Smolders GJ, Vandermeij J, Vanloosdrecht MC, Heijnen JJ, Biotechnol. Bioeng., 43(6), 461 (1994)
Kumar BM, Chaudhari S, Water Sci. Technol., 48(3), 73 (2003)
Filipe CDM, Daigger GT, Grady CPL, Biotechnol. Bioeng., 76(1), 17 (2001)
Filipe CDM, Daigger GT, Grady CLP, Water Environ. Res., 73(2), 213 (2001)
Feng HPH, Zhang T, Liu Y, Water Res., 36(13), 3211 (2002)