首页> 外文期刊>Ecological engineering: The Journal of Ecotechnology >Comparative study of nitrogen removal and bio-film clogging for three filter media packing strategies in vertical flow constructed wetlands
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Comparative study of nitrogen removal and bio-film clogging for three filter media packing strategies in vertical flow constructed wetlands

机译:垂直流人工湿地中三种滤料填充策略的脱氮和生物膜堵塞比较研究

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This study investigated the discrepancies in nitrogen removal and clogging for vertical flow constructed wetlands (VFCWs) using different packing strategies. Parallel lab-scale VFCWs reactors were created and packed with quartz sand filter media. Three packing strategies were adopted: increasing-sized (I-packing), decreasing-sized (D-packing) and uniform-sized (U-packing) packing. The clogging rate coefficient and biomass accumulation rate were defined to assess clogging. The results demonstrated that the nitrogen removal was highest for the I-packing reactor at 43%. The ammonia and COD removal rates reached 56% and 64%, respectively. I-packing reactor presented an aerobic-to-anoxic transition area, where DO ranged from 4.6 to 0.3 mg/L. Such condition is ideal for the nitrification and denitrification reaction. Clogging is primarily the result of the rapid reduction of the effective porosity due to bio-film growth. Clogging is related to the position of biomass accumulation, while the reduction of the internal void space is not the determining factor for the I-packing reactor. The clogging rate of the I-packing reactor much lower than D-packing and U-packing reactors. Bed resting between operations can be used for clogging mitigation and system recovery, but this approach was not effective for D-packing. The I-packing reactor was proven to be the most efficient for nitrogen removal and showed the strongest clogging prevention capability. (C) 2014 Elsevier B.V. All rights reserved.
机译:本研究调查了采用不同包装策略的垂直流人工湿地(VFCW)的脱氮和堵塞氮差异。创建了平行实验室规模的VFCWs反应堆,并用石英砂滤料填充。采用了三种包装策略:增大尺寸(I型包装),减小尺寸(D型包装)和均匀尺寸(U型包装)。定义堵塞率系数和生物量积累率以评估堵塞。结果表明,对于I装填反应器,脱氮率最高,为43%。氨和COD去除率分别达到56%和64%。工装反应器呈现出有氧至缺氧的过渡区域,其中DO范围为4.6至0.3 mg / L。这种条件对于硝化和反硝化反应是理想的。堵塞主要是由于生物膜生长导致有效孔隙率快速降低的结果。堵塞与生物质积累的位置有关,而内部空隙空间的减少不是I型填充反应器的决定因素。 I型填料反应器的堵塞率远低于D型填料反应器和U型填料反应器。两次手术之间的卧床休息可用于缓解堵塞和恢复系统,但这种方法对D型包装无效。事实证明,I型填充反应器是最有效的脱氮方法,具有最强的防堵塞能力。 (C)2014 Elsevier B.V.保留所有权利。

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