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Flow characteristic and wastewater treatment
performance of a pilot-scale airlift oxidation ditch |
Hongtao PANG,Hanchang SHI,Huiming SHI, |
Department of Environmental
Science and Engineering, Tsinghua University, Beijing 100084, China; |
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Abstract A pilot-scale airlift oxidation ditch using bubble diffuser and baffle as aerator was operated in a wastewater treatment plant (WWTP) to investigate its flow characteristic and wastewater treatment performance. Compared with the conventional oxidation ditch process, effective depth and oxygen utilization efficiency of this new process was improved by underwater aeration. Furthermore, it had a reversed velocity distribution, which decreased from the bottom to the top on vertical section. Velocity measurement showed that a velocity over 0.2m/s at the bottom was sufficient to prevent sludge settlement during long term operation. Application of these concepts would save land area and energy consumption by about 25%―50% and 55%, respectively. In this new system, organic biodegradation and nitrification could be well achieved. Denitrification could occur steadily in the straight part by adjusting the airflow rate. An average TN removal rate of 63% was achieved with dissolved oxygen (DO) concentrations between 0.6mg/L and 1.5mg/L. The main pollutants in the effluent could meet the strictest discharge standard (COD<50mg/L, NH4+―N<5mg/L, and TN<15mg/L) in China now.
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Keywords
airlift oxidation ditch
flow characteristic
wastewater treatment
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Issue Date: 05 December 2009
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Barnes D, Forster C F, Johnstone D W M. Oxidation Ditches in Wastewater Treatment. London: PitmanBooks limited, 1983
|
|
Mandt M G, Bell B A. Oxidation Ditches in WastewaterTreatment. Collingwood: Ann Arbor Science Publishers, 1984
|
|
US Environmental Protection Agency, Officeof Water. EPA 832-F-00-013 Wastewater TechnologyFact Sheet: Oxidation Ditches. 2000
|
|
Gillot S, Capela S, Héduit A. Effect of horizontal flow on oxygen transferin clean water with surfactants. WaterResearch, 2000, 34 (2): 678―683
doi: 10.1016/S0043-1354(99)00167-0
|
|
Nicolella C, van Loosdrecht MC M, Heijnen J J. Mass transfer and reactionin a biofilm airlift suspension reactor. Chemical Engineering Science, 1998, 53(15): 2743―2753
doi: 10.1016/S0009-2509(98)00107-9
|
|
Talvy S, Cockx A, Line A. Global modeling of a gas–liquid–solid airliftreactor. Chemical Engineering Science, 2005, 60(22): 5991―6003
doi: 10.1016/j.ces.2005.04.067
|
|
Shi H C, Yin Y M. China Patent.200510008928.5, 2005
|
|
Environmental Protection Agency of JiangsuProvince, China. Discharge standard of mainwater pollutants for municipal wastewater treatment plant of Taihuarea (DB32/1072-2007) (in Chinese)
|
|
State Environmental Protection Agency, China. Standard Methods for the Examination of Water and Wastewater. 4th ed. Beijing: Chinese Environmental Science Publishers, 2002 (in Chinese)
|
|
Pang H T, Shi H C, Shi H M, Yang C, Yin Y M. Flow characteristic of a pilot scaleairlift oxidation ditch. China EnvironmentalScience, 2008, 28(12): 1057―1061 (in Chinese)
|
|
Argaman Y. Singlesludge nitrogen removal in an oxidation ditch. Water Research, 1984, 18 (1): 493―500
doi: 10.1016/0043-1354(84)90123-4
|
|
Rittman B E, Langeland W E. Simultaneous denitrificationwith nitrification in single-channel oxidation ditches. Journal of the Water Pollution Control Federation, 1985, 57(4): 300―308
|
|
Liu J X, Groenestijn J W, Doddema H J, Wang B Z. Influenceof the aeration brush on nitrogen removal in the oxidation ditch. European Water Pollution Control, 1996, 6: 25―30
|
|
Hao X D, Doddema H J, Van Groenestijn J W. Conditions and mechanisms affecting simultaneousnitrification and denitrification in a pasveer oxidation ditch. Bioresource Technology, 1997, 59: 207―215
doi: 10.1016/S0960-8524(96)00143-5
|
|
Holman J B, Wareham D G. COD, ammonia and dissolvedoxygen time profiles in the simultaneous nitrification/denitrificationprocess. Biochemical Engineering Journal, 2005, 22: 125―133
doi: 10.1016/j.bej.2004.09.001
|
|
Pochana K, Keller J. Study of factors affectingsimultaneous nitrification and denitrification (SND). Water Science and Technology, 1999, 39 (6): 61―68
doi: 10.1016/S0273-1223(99)00123-7
|
|
Collivignarelli C, Bertanza G. Simultaneous nitrification-denitrificationprocesses in activated sludge plants performance and applicability. Water Science and Technology, 1999, 40(4-5): 187―194
doi: 10.1016/S0273-1223(99)00575-2
|
|
Peng Y Z, Hou H X, Wang S Y. Nitrogen and phosphorus removal in pilot-scale anaerobic-anoxicoxidation ditch system. Journal of EnvironmentalSciences, 2008, 20(4): 398―403
doi: 10.1016/S1001-0742(08)62070-7
|
|
Liu Y C, Shi H C, Wang Z Q. Variation of dissolved oxygen and optimum control conditionsin carrousel oxidation ditch. China EnvironmentalScience, 2008, 28(9): 843―846 (in Chinese)
|
|
Gillot S, Capela S, Heduit A. Effect of horizontal flow on oxygen transfer in cleanwater with surfactants. Water Research, 2000, 34(2): 678―683
doi: 10.1016/S0043-1354(99)00167-0
|
|
Gillot S, Heduit A. Effect of air flow rate onoxygen transfer in an oxidation ditch equipped with fine bubble diffusersand slow speed mixers. Water Research, 2000, 34(5): 1756―1762
doi: 10.1016/S0043-1354(99)00323-1
|
|
Nakasone H, Ozaki M. Oxidation-ditch process usingfalling water as aerator. Journal of EnvironmentalEngineering, 1995, 121(2): 132―139
doi: 10.1061/(ASCE)0733-9372(1995)121:2(132)
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