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In relation to this article, we declare that there is no conflict of interest.
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Received March 18, 2005
Accepted June 10, 2005
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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Control and Nitrogen Load Estimation of Aerobic Stage in Full-Scale Sequencing Batch Reactor to Treat Strong Nitrogen Swine Wastewater

Water Environment & Remediation Center, Korea Institute of Science and Technology, 39-1, Hawolkok-dong, Seongbuk-gu, Seoul 136-791, Korea 1Dept. of Environmental Engineering, Pusan National University, San 30, Jangjun-dong, Keumjung-gu, Busan 609-735, Korea
cwkim@pusan.ac.kr
Korean Journal of Chemical Engineering, September 2005, 22(5), 666-670(5), 10.1007/BF02705780
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Abstract

Three different control methods based on oxidation reduction potential (ORP) and dissolved oxygen (DO) for determining aeration time were evaluated for swine wastewater treatment at full-scale SBR. For determining the Ending Point of Ammonia Oxidation (EPAO), the plateau in ORP profile, the derivative of DO, and absolute DO were tested. Below 0.5 kg NH4_x000D_ +-N/m3·day of influent loading rate, three control methods produced good results; however, above this loading rate, only absolute DO method was feasible. The volumetric ammonia nitrogen load at the sub-cycle (Kg NH4 +-N/m3/sub-cycle) had an effect on the period of aeration. To put it more concretely, the higher loading rate required a longer ammonia nitrogen oxidation period. To estimate nitrogen load, the length of low DO period, which was defined as the required time to reach 3 mg DO/l from the start of aeration, was the most proper parameter.

References

Al-Ghusain IA, Hao OJ, J. Environ. Eng.-ASCE, 121(3), 225 (1995) 
Andreottola G, Foladori P, Ragazzi M, Water Sci. Technol., 43(3), 93 (2001)
Paul E, Plisson SS, Mauret M, Cantet J, Water Sci. Technol., 38(3), 299 (1998) 
Plisson SS, Capdeville B, Mauret M, Deguin A, Baptiste P, Water Sci. Technol., 33(1), 275 (1996) 
Poo KM, Jun BH, Lee SH, Woo JH, Kim CW, Water Sci. Technol., 49(5-6), 315 (2004)
Yoo CK, Lee JM, Lee IB, Korean J. Chem. Eng., 21(1), 14 (2004)
Zipper T, Fleischmann N, Haberl R, Water Sci. Technol., 38(3), 307 (1998) 

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