Kinetics of nitrogen removal in high rate anammox upflow filter

被引:66
作者
Jin, Ren-Cun [1 ,2 ]
Zheng, Ping [2 ]
机构
[1] Hangzhou Normal Univ, Dept Environm Sci, Hangzhou 310036, Zhejiang, Peoples R China
[2] Zhejiang Univ, Dept Environm Engn, Hangzhou 310029, Zhejiang, Peoples R China
关键词
Anammox; Upflow anaerobic filter; Kinetic; Modeling; Nitrogen removal; AMMONIUM OXIDATION ANAMMOX; WASTE-WATER; ANAEROBIC FILTER; START-UP; REACTOR; PERFORMANCE; BACTERIA; COLUMN;
D O I
10.1016/j.jhazmat.2009.05.016
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The process kinetics for laboratory-scale anammox (anaerobic ammonium oxidation) upflow filter using synthetic wastewater as feed were investigated. The experimental unit consisted of a 2.0L reactor filled with three-dimensional plastic media. The filter was tested for different influent substrate concentrations and hydraulic retention time (HRT). The substrate loading removal rate was compared with prediction of Stover-Kincannon, second-order and the first-order substrate removal models. Upon approaching pseudo-steady-state condition, substrate ammonium or nitrite concentrations were increased from 280 to 462 mg N/L,while HRT was stepwise decreased from 14.4 to 2 h,with a concomitant increase in nitrogen loading rate (NLR) from 0.93 to 7.34 g/L day. Based on calculations, Stover-Kincannon model and second-order "Grau" model were found to be the appropriate models to describe the upflow filter. According to Stover-Kincan non model, the maximum total substrate removal rate constant (U-max) and saturation value constant (K-B) were suggested as 12.4 and 12.0g N/L day, respectively. As Stover-Kincannon model and second-order model gave high correlation coefficients (97.9% and 98.6%, respectively). these models may be used in predicting the behavior or design of the anammox filter. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:652 / 656
页数:5
相关论文
共 35 条
[1]   Kinetic analyses of the operation of mesophilic and thermophilic anaerobic filters treating a simulated starch wastewater [J].
Ahn, JH ;
Forster, CF .
PROCESS BIOCHEMISTRY, 2000, 36 (1-2) :19-23
[2]  
Ahn JH, 2002, PROCESS BIOCHEM, V38, P257
[3]  
*APHA WWA WEF, 1998, STAND METH WAT WAST
[4]   Aerobic purification of dairy wastewater in continuous regime Part II:: Kinetic study of the organic matter removal in two reactor configurations [J].
Carta-Escobar, F ;
Pereda-Marín, J ;
Alvarez-Mateos, P ;
Romero-Guzmán, F ;
Barrantes, MMD .
BIOCHEMICAL ENGINEERING JOURNAL, 2005, 22 (02) :117-124
[5]   Biogeographical distribution of diverse anaerobic ammonium oxidizing (anammox) bacteria in Cape Fear River Estuary [J].
Dale, Olivia R. ;
Tobias, Craig R. ;
Song, Bongkeun .
ENVIRONMENTAL MICROBIOLOGY, 2009, 11 (05) :1194-1207
[6]   N2 production by the anammox reaction in the anoxic water column of Golfo Dulce, Costa Rica [J].
Dalsgaard, T ;
Canfield, DE ;
Petersen, J ;
Thamdrup, B ;
Acuña-González, J .
NATURE, 2003, 422 (6932) :606-608
[7]   Anammox process for nitrogen removal from anaerobically digested fish canning effluents [J].
Dapena-Mora, A. ;
Campos, J. L. ;
Mosquera-Corral, A. ;
Mendez, R. .
WATER SCIENCE AND TECHNOLOGY, 2006, 53 (12) :265-274
[8]   Enrichment and characterization of an anammox bacterium from a rotating biological contactor treating ammonium-rich leachate [J].
Egli, K ;
Fanger, U ;
Alvarez, PJJ ;
Siegrist, H ;
van der Meer, JR ;
Zehnder, AJB .
ARCHIVES OF MICROBIOLOGY, 2001, 175 (03) :198-207
[9]   Mass cultivation of anaerobic ammonium-oxidizing sludge using a novel nonwoven biomass carrier [J].
Furukawa, K ;
Rouse, JD ;
Yoshida, N ;
Hatanaka, H .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2003, 36 (10) :1163-1169
[10]   Biological treatment of ammonium-rich wastewater by partial nitritation and subsequent anaerobic ammonium oxidation (anammox) in a pilot plant [J].
Fux, C ;
Boehler, M ;
Huber, P ;
Brunner, I ;
Siegrist, H .
JOURNAL OF BIOTECHNOLOGY, 2002, 99 (03) :295-306