Impacts of temperature and nitrifying community on nitrification kinetics in a moving-bed biofilm reactor treating polluted raw water

被引:114
作者
Zhang, Shuangfu [1 ]
Wang, Yayi [1 ]
He, Weitao [1 ]
Wu, Min [1 ]
Xing, Meiyan [1 ]
Yang, Jian [1 ]
Gao, Naiyun [1 ]
Pan, Mianli [2 ]
机构
[1] Tongji Univ, Coll Environm Sci & Engn, State Key Lab Pollut Control & Resources Reuse, Shanghai 200092, Peoples R China
[2] Shanghai Inst Pharmaceut Ind, Ctr Pharmacol Evaluat, Shanghai 200040, Peoples R China
基金
中国国家自然科学基金;
关键词
Polluted raw water; Moving-bed biofilm reactor; Temperature; Nitrifying community; Temperature coefficient; Nitrification kinetics; IN-SITU ANALYSIS; BIOLOGICAL TREATMENT; NITROGEN REMOVAL; WASTE-WATER; BACTERIA; PRETREATMENT; NITRITE; RATES; PH;
D O I
10.1016/j.cej.2013.09.086
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Although nitrification kinetics have been widely studied in wastewater treatment systems to optimize the design and operation of the nitrification process, more information is still needed to fully understand the kinetics of moving-bed biofilm reactors (MBBRs) used for biological pretreatment of low ammonia concentration polluted raw water. In this study, nitrification kinetics of a pilot-scale MBBR treating polluted raw water were studied while focusing on the impacts of temperature and the nitrifying community. Nitrification batch tests were conducted with an initial ammonia concentration of 2.0 mg L-1 and varying raw water temperatures of 2.8-28.3 degrees C. The oxidation rates of ammonia and nitrite increased with temperature, although the biomass concentrations decreased from 348.7 to 188.9 mg VS L-1 as temperature increased from 16.1 to 28.3 degrees C. The specific ammonia and nitrite oxidation rates were also highly dependent on temperature. Because of severe inhibition at temperatures below 5.0 degrees C, the temperature impacts were calibrated by eliminating the kinetic data measured below 5.0 degrees C Moreover, the variations in functional microorganisms for AOB (beta-Proteobacterial AOB) and NOB (Nitrobacter spp.) were normalized for the modified nitrification kinetics. Thus, the final temperature coefficients were 1.099 and 1.098 for ammonia and nitrite oxidation kinetics, respectively, demonstrating the temperature impacts on nitrification kinetics in MBBRs treating polluted raw water. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:242 / 250
页数:9
相关论文
共 34 条
[1]  
Barnes D., 1983, BIOL CONTROL NITROGE
[2]   Effect of Different Operational Conditions on Biofilm Development, Nitrification, and Nitrifying Microbial Population in Moving-Bed Biofilm Reactors [J].
Bassin, J. P. ;
Kleerebezem, R. ;
Rosado, A. S. ;
van Loosdrecht, M. C. M. ;
Dezotti, M. .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2012, 46 (03) :1546-1555
[3]  
Chinese SEPA, 2002, WAT WAST WAT MON MET, Vfourth
[4]   Bio-diatomite dynamic membrane reactor for micro-polluted surface water treatment [J].
Chu, Huaqiang ;
Cao, Dawen ;
Dong, Bingzhi ;
Qiang, Zhimin .
WATER RESEARCH, 2010, 44 (05) :1573-1579
[5]   Impacts of drinking water pretreatments on the formation of nitrogenous disinfection by-products [J].
Chu, Wenhai ;
Gao, Naiyun ;
Deng, Yang ;
Templeton, Michael R. ;
Yin, Daqiang .
BIORESOURCE TECHNOLOGY, 2011, 102 (24) :11161-11166
[6]   Chlorination of natural organic matter: kinetics of chlorination and of THM formation [J].
Gallard, H ;
von Gunten, U .
WATER RESEARCH, 2002, 36 (01) :65-74
[7]   AMMONIA OXIDATION IN NITROSOMONAS AT NH3 CONCENTRATIONS NEAR K-M - EFFECTS OF PH AND TEMPERATURE [J].
GROENEWEG, J ;
SELLNER, B ;
TAPPE, W .
WATER RESEARCH, 1994, 28 (12) :2561-2566
[8]   NITRIFICATION IN A MOVING-BED BIOFILM REACTOR [J].
HEM, LJ ;
RUSTEN, B ;
ODEGAARD, H .
WATER RESEARCH, 1994, 28 (06) :1425-1433
[9]   Phylogenetic probes for analyzing abundance and spatial organization of nitrifying bacteria [J].
Mobarry, BK ;
Wagner, M ;
Urbain, V ;
Rittmann, BE ;
Stahl, DA .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 1996, 62 (06) :2156-2162
[10]  
Odegaard H., 1993, 9TH P EWPCA ISWA S M, P205