Nitrogen removal performances of a polyvinylidene fluoride membrane-aerated biofilm reactor

被引:33
|
作者
Lin, Jiayi [1 ]
Zhang, Panyue [1 ]
Yin, Jiang [1 ]
Zhao, Xuehao [1 ]
Li, Juan [1 ]
机构
[1] Beijing Forestry Univ, Beijing Key Lab Source Control Technol Water Poll, Coll Environm Sci & Engn, Beijing 100083, Peoples R China
关键词
Membrane-aerated biofilm reactor; Nitrogen removal; Simultaneous nitrification and denitrification; Microbial communities; Anaerobic ammonium oxidation; WASTE-WATER TREATMENT; MICROBIAL COMMUNITY; ACTIVATED-SLUDGE; TREATMENT-PLANT; BACTERIA; CARBON; NITRIFICATION; ANAMMOX; SYSTEM; MABR;
D O I
10.1016/j.ibiod.2015.01.013
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
A membrane-aerated biofilm reactor (MABR) with polyvinylidene fluoride (PVDF) hollow fiber membranes was developed, and the nitrogen removal performances with the increase of influent NH4+ - N concentration from 30 mg/L to 120 mg/L were investigated. The results indicated that simultaneous nitrification and denitrification (SND) process was realized in this MABR system, and the nitrogen removal performances were affected by the influent NH4+ - N concentration. The limitation of influent NH4+ - N concentration for this MABR system was 70 mg/L with a maximum specific NH4+ - N conversion rate and specific total nitrogen removal rate of 55.67 and 52.87 kg/m(3) d, showing better performances compared with other studies. The nitrogen removal was realized through nitrification, denitrification and possible anaerobic ammonium oxidation (ANAMMOX) with partial nitrification. The polymerase chain reaction-denaturing gradient gel electrophoresis (PCR-DGGE) was used to analyze the microbial community of biofilm in this MABR system, revealing the bacteria community diversity of biofilm. Besides various ammonia-oxidizing bacteria and nitrite-oxidizing bacteria, Nitrosomonas sp. and Planctomycetes sp. were found to conduct ANAMMOX with partial nitrification under oxygen limited condition. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:49 / 55
页数:7
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