Influences of COD Model Components in ASM2D on Oxygen Mass Transfer Coefficient

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Chemical Oxygen Demand was split into SA (volatile acid / fermentation products), SF (fermentable, readily bio-degradable organic substrates), XS (slowly biodegradable substrates), SI (Inert soluble organic material) and XI (Inert particulate organic material). Research of how these model components affect the oxygen transfer coefficient (KLa) was studied in this paper. The results showed that with the increase of SA, KLa decreased, KLa first decreased when SF was in 25-100 mgCOD/L, then it increased in 100-200 mg/L,then it decreased again. XS has a poor regularity and slight infect on oxygen mass transfer, XI, SI may inhibit the oxygen transfer.

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347-351

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September 2013

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© 2013 Trans Tech Publications Ltd. All Rights Reserved

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[1] X. Liu. Study of main factors affecting the oxygen mass transfer in aeration technology [D]. DaLian: Dalian University of Technology, (2008).

Google Scholar

[2] L.P. Zhou, H.T. Zhao, Z.R. Liu, et al. Research on the effects of water quality on the oxygen mass transfer [J]. Journal of North University of China, 2010, 31(1): 45-49.

Google Scholar

[3] Marupatch Jamnongwong, Nicolas Dietrich, Gilles Hébrard et al. Experimental study of oxygen diffusion coefficients in clean water containing salt, glucose or surfactant: Consequences on the liquid-side mass transfer coefficients[J]. Chemical Engineering Journal, 2010, 165: 758-768.

DOI: 10.1016/j.cej.2010.09.040

Google Scholar

[4] F. Garcı´a-Ochoa, E. Go´ mez Castro. Estimation of oxygen mass transfer coefficient in stirred tank reactors using artificial neural networks [J]. Enzyme and Microbial Technology, 2001, 28: 560-569.

DOI: 10.1016/s0141-0229(01)00297-6

Google Scholar

[5] Belma Ozbek, Sevgi Gayik. The studies on the oxygen mass transfer coefficient in a bioreactor[J], Process Biochemistry 2001, 36: 729-741.

DOI: 10.1016/s0032-9592(00)00272-7

Google Scholar

[6] J.H. Sun, J.L. Gao, Y. Shi, et al. Research on the effects of COD on total oxygen transfer coefficient [J]. Industrial water treatment, 2011, 31(11): 31-33.

Google Scholar

[7] GB11914-89, Determination of COD-dichromate method [S].

Google Scholar

[8] HJ_505-2009, Determination of biochemical oxygen demand after 5 days (BOD5) for dilution and seeding method [S].

Google Scholar

[9] HJ 636-2012, Determination of total nitrogen-Alkaline potassium persulfate digestion UV spectrophotometric method[S].

Google Scholar

[10] GB11893-89, Determination of total phosphorus-Ammonium molybdate spec- trophotometric method[S].

Google Scholar

[11] GB11901-89, Determination of suspended substance-Gravimetric method[S].

Google Scholar

[12] Mogens Henze, Willi Gujer, Takahashi Mino et al. Activated sludge modle NO. 2D, ASM2D[J]. water sci. Tech. 1999, 39(1): 165-182.

DOI: 10.2166/wst.1999.0036

Google Scholar

[13] X.F. Gu, H.Z. Yang. Determination of the organic components in ASM2 [D]. ShangHai: Tongji University, (2005).

Google Scholar

[14] Z.J. Zhang. Drainage engineering [M]. 4 Edition. Beijing: China building industry press, 2002: 146-147.

Google Scholar

[15] Beijing municipal engineering design & research institute.Water supply and drainage design manual:5 copies [M].2 Edition. Beijing: China building industry press, 2004: 908.

Google Scholar