Simultaneous nitrogen and phosphorus removal by combined anammox and denitrifying phosphorus removal process

被引:31
|
作者
Zhang, Meijiao [1 ]
Qiao, Sen [1 ]
Shao, Donghai [2 ]
Jin, Ruofei [1 ]
Zhou, Jiti [1 ]
机构
[1] Dalian Univ Technol, Sch Environm Sci & Technol, Key Lab Ind Ecol & Environm Engn, Minist Educ, Dalian 116024, Peoples R China
[2] Dalian Environm Engn Assessment Ctr, Dalian, Peoples R China
关键词
SNAP process; DPAO process; DPAO-SNAP process; carbon sources; POLYPHOSPHATE-ACCUMULATING ORGANISMS; SIMULTANEOUS PARTIAL NITRIFICATION; DENITRIFICATION SNAD PROCESS; MICROBIAL COMMUNITY; START-UP; CANDIDATUS-ACCUMULIBACTER; NITRITATION-ANAMMOX; WASTE-WATER; SLUDGE; REACTOR;
D O I
10.1002/jctb.5326
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
BACKGROUNDSingle-stage nitrogen removal using anammox and partial nitrification process (SNAP process) is a promising process to treat low C/N wastewater relying on ammonia-oxidizing bacteria (AOB) and anaerobic ammonium oxidation (anammox) bacteria. However, excess nitrate (NO3-) in effluent is a common problem for the SNAP process. The denitrifying phosphorus removal (DPAO) process using NO3- as electron acceptor was adopted to reduce nitrate in effluent from the SNAP process, while phosphorus removal was also achieved simultaneously. Thus, a novel combined process (DPAO-SNAP process) was established to achieve nitrogen and phosphorus removal simultaneously. RESULTSThe DPAO-SNAP process achieved average 95.7% chemical oxygen demand, 98.2% total nitrogen and 97.8% total phosphorus removal efficiencies during stable stages. Furthermore, Candidatus Kuenenia and Nitrosomonas were identified as the dominant genus for anammox bacteria and AOB, respectively. Defluviicoccus was enriched as the glycogen-accumulating microorganism (GAOs) for the DPAO process with acetate as the carbon source, while Rhodocyclales was the dominant genus in the DPAO process with mixed carbon source. CONCLUSIONThis DPAO-SNAP process could not only resolve the problem of effluent NO3- in the SNAP process but also simultaneously achieved high removal efficiency of COD, TN and TP with a low need for carbon sources (COD/N/P=25:15:1). (c) 2017 Society of Chemical Industry
引用
收藏
页码:94 / 104
页数:11
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