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HYDRODYNAMIC BEHAVIOUR OF A FULL-SCALE SUBMERGED BIOFILTER AND ITS POSSIBLE INFLUENCE ON PERFORMANCES

机译:大型浸入式生物滤池的水动力特性及其对性能的影响

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The hydrodynamic behaviour of a 110 m~2 full-scale submerged upflow biofilter, filled with 2.8 m of floating media and used for tertiary nitrification of treated domestic sewage was investigated. Residence time distributions were obtained from lithium chloride tracer experiments. Four trials were performed at 3.7 and 6.5-6.7 mh~(-1), once without aeration. Spatial differences in the mean residence time of a given cross-section were in the range of 30-40% and can be attributed to the distribution system of the influent at the bottom of the filter. Sampling at the bottom and top of the filter bed media showed that the behaviour of the filter bed itself is close to a dispersed plug flow reactor. The dispersion lengths are in the range 60-100 mm, increase with flow rate and are unaffected by the aeration. From simple model calculations, it was concluded that the heterogeneity observed within the filter bed would have no significant effect on water quality. Heterogeneity due to the distribution of effluent in the lower part of the filter would also have a very limited effect in the case of sudden changes in the effluent substrate concentration.
机译:研究了一个110 m〜2的全尺寸浸没式上流式生物滤池的水动力行为,该滤池装有2.8 m的悬浮介质,用于处理的生活污水的三次硝化。从氯化锂示踪剂实验获得停留时间分布。四次试验分别在3.7和6.5-6.7 mh〜(-1)下进行,一次不充气。给定横截面的平均停留时间的空间差异在30%至40%的范围内,这可以归因于过滤器底部进水口的分配系统。在滤床介质的底部和顶部取样表明,滤床本身的行为接近分散的活塞流反应器。分散体的长度在60-100 mm范围内,随流速增加而不受充气的影响。从简单的模型计算可以得出结论,滤床内观察到的异质性不会对水质产生重大影响。在流出物底物浓度突然变化的情况下,由于流出物在过滤器下部的分布所造成的异质性也将具有非常有限的影响。

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