首页> 外文会议>The International Conference on Advances in Chemical Technologies for Water and Wastewater Treatment(2008年化学技术对水及废水处理国际研讨会)论文集 >Experimental study on denitrification efficiency impacted by activated sludge filtering bed formed in gas-liquid-solid separating zone
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Experimental study on denitrification efficiency impacted by activated sludge filtering bed formed in gas-liquid-solid separating zone

机译:气液固分离区形成的活性污泥滤床影响反硝化效率的实验研究

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The experimental study on denitrificaiton of nitrogenous organic wastewater using the co-processes of bio-fluidized bed plus activated sludge filter bed which formed in gas-1iquid-solid separating zone was carried out.Experimental results showed that:1) Non-suppressed nitrification bacteria group by carbon sources was reproduced in the Bio-nuidized bed system.which in turn contributed to the NH4+-N removal efficiency of up to 93%~95%;2)Dynamic and stable sludge filter was formed in the gas-liquid-solid separating zone by the setting of incline-tube and the controlling of precipitation mud condition,Which leaded to the dramatically improving of TN removal rate:3)85%BOD5 removal efficiency and 74%TN removal efficiency was achieved under the operation conditions of HRT Of 1.5h.Aeration of0.25 m3h-3,BOD5 load of 9.2-10.4 m-3d-3 and TN load ofO.65 kgm-3d-1.
机译:进行了在气固两相分离区中形成的生物流化床与活性污泥滤床协同处理含氮有机废水的反硝化实验研究。实验结果表明:1)非抑制型硝化细菌在生物硝化床系统中复制了按碳源分类的碳源,从而使NH4 + -N的去除率高达93%〜95%; 2)在气液固中形成了动态稳定的污泥过滤器通过设置斜管和沉淀泥条件控制分离区,从而显着提高了总氮的去除率:3)在HRT运行条件下,总氮的去除率达到85%,BOD5的去除率达到了74%。 1.5h。通气量为0.25 m3h-3,BOD5负荷为9.2-10.4 m-3d-3,TN负荷为O.65 kgm-3d-1。

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