Biological nitrogen and carbon removal in a gravity flow biomass concentrator reactor for municipal sewage treatment

被引:11
|
作者
Scott, Daniel [1 ]
Hidaka, Taira [1 ,4 ]
Campo, Pablo [1 ]
Kleiner, Eric [2 ]
Suidan, Makram T. [3 ]
Venosa, Albert D. [2 ]
机构
[1] Univ Cincinnati, Sch Energy Environm Biol & Med Engn, Cincinnati, OH 45221 USA
[2] NRMRL USEPA, Cincinnati, OH 45268 USA
[3] Amer Univ Beirut, Deans Off, Fac Engn & Architecture, Beirut 11072020, Lebanon
[4] Kyoto Univ, Dept Environm Engn, Nishikyo Ku, Kyoto 6158540, Japan
关键词
Biomass concentrator reactor; Membrane filtration; Gravity flow; Solids retention times; Nitrogen removal; NUTRIENT REMOVAL; MTBE;
D O I
10.1016/j.chemosphere.2012.08.045
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A novel membrane system, the Biomass Concentrator Reactor (BCR), was evaluated as an alternative technology for the treatment of municipal wastewater. Because the BCR is equipped with a membrane whose average poresize is 20 mu m (18-28 mu m), the reactor requires low-pressure differential to operate (gravity). The effectiveness of this system was evaluated for the removal of carbon and nitrogen using two identical BCRs, identified as conventional and hybrid, that were operated in parallel. The conventional reactor was operated under full aerobic conditions (i.e., organic carbon and ammonia oxidation), while the hybrid reactor incorporated an anoxic zone for nitrate reduction as well as an aerobic zone for organic carbon and ammonia oxidation. Both reactors were fed synthetic wastewater at a flow rate of 71 L d(-1), which resulted in a hydraulic retention time of 9 h. In the case of the hybrid reactor, the recycle flow from the aerobic zone to the anoxic zone was twice the feed flow rate. Reactor performance was evaluated under two solids retention times (6 and 15 d). Under these conditions, the BCRs achieved nearly 100% mixed liquor solids separation with a hydraulic head differential of less than 2.5 cm. The COD removal efficiency was over 90%. Essentially complete nitrification was achieved in both systems, and nitrogen removal in the hybrid reactor was close to the expected value (67%). (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1412 / 1418
页数:7
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