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

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Indexed by:期刊论文

First Author:Zhang, Meijiao

Correspondence Author:Qiao, S (reprint author), Dalian Univ Technol, Sch Environm Sci & Technol, Key Lab Ind Ecol & Environm Engn, Minist Educ, Dalian 116024, Peoples R China.

Co-author:Qiao, Sen,Shao, Donghai,Jin, Ruofei,Zhou, Jiti

Date of Publication:2018-01-01

Journal:JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY

Included Journals:SCIE、EI、Scopus

Volume:93

Issue:1

Page Number:94-104

ISSN No.:0268-2575

Key Words:SNAP process; DPAO process; DPAO-SNAP process; carbon sources

Abstract: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

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