Complete nitrogen removal from municipal wastewater via partial nitrification by appropriately alternating anoxic/aerobic conditions in a continuous plug-flow step feed process

被引:188
|
作者
Ge, Shijian [1 ]
Peng, Yongzhen [1 ]
Qiu, Shuang [2 ]
Zhu, Ao [1 ]
Ren, Nanqi [3 ]
机构
[1] Beijing Univ Technol, Engn Res Ctr Beijing, Key Lab Beijing Water Qual Sci & Water Environm R, Beijing 100124, Peoples R China
[2] SUNY Upstate Med Univ, Coll Grad Studies, Syracuse, NY 13210 USA
[3] Harbin Inst Technol, State Key Lab Urban Water Resource & Environm, Harbin 150090, Peoples R China
基金
国家高技术研究发展计划(863计划);
关键词
Partial nitrification; Nitritation; Biological nutrient removal; Wastewater; Step feed; ENHANCED NUTRIENT REMOVAL; LOW DISSOLVED-OXYGEN; NITROSOMONAS-EUROPAEA; NITRITE ACCUMULATION; OXIDIZING BACTERIA; REACTOR; COMMUNITY; AMMONIA; SCALE; DENITRITATION;
D O I
10.1016/j.watres.2014.01.058
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This study assessed the technical feasibility of removing nitrogen from municipal wastewater by partial nitrification (nitritation) in a continuous plug-flow step feed process. Nitrite in the effluent accumulated to over 81.5 +/- 9.2% but disappeared with the transition of process operation from anoxic/oxic mode to the anaerobic/anoxic/oxic mode. Batch tests showed obvious ammonia oxidizing bacteria (AOB) stimulation (advanced ammonia oxidation rate) and nitrite (NOB) oxidizing bacteria inhibition (reduced nitrite oxidation rate) under transient anoxic conditions. Two main factors contributed to nitritation in this continuous plug-flow process: One was the alternating anoxic and oxic operational condition; the step feed strategy guaranteed timely denitrification in anoxic zones, allowing a reduction in energy supply (nitrite) to NOB. Fluorescence in Situ Hybridization and quantitative real-time polymerase chain reaction analysis indicated that NOB population gradually decreased to 1.0 +/- 0.1% of the total bacterial population (dominant Nitrospira spp., 1.55 x 10(9) copies/L) while AOB increased approximately two-fold (7.4 +/- 0.9%, 1.25 x 10(10) copies/L) during the above anoxic to anaerobic transition. Most importantly, without addition of external carbon sources, the above wastewater treatment process reached 86.0 +/- 4.2% of total nitrogen (TN) removal with only 7.23 +/- 2.31 mg/L of TN in the effluent, which met the discharge requirements. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:95 / 105
页数:11
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