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PERFORMANCE OF FLOATING AND SUNKEN MEDIA BIOLOGICAL AERATED FILTERS UNDER UNSTEADY STATE CONDITIONS

机译:非稳态条件下漂浮和沉没的介质生物曝气滤池的性能

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The biological aerated filter (BAF) combines both biological treatment and solids removal in one submerged, aerated three phase reactor. Over the last 20 yr biological aerated filters have been developed not only as competitors for other secondary treatment systems such as trickling filters and activated sludge plants but also as tertiary treatment systems. The aim of this work was to compare the performance of two such reactors, one containing a floating media and the other containing a sunken media under identical conditions during start-up and with increasing hydraulic flowrates. Two methods of start-up were used. The first method used activated sludge as seed which was recycled through the reactor, the second method involved simply passing the process liquid (settled domestic sewage) through the reactor at the initial flowrate. Following a period of steady-state the flowrates were increased incre- mentally and the performance of the reactors analysed during and after each increase. The results for the start-up indicated that the overall time to reach steady-state using both methods was approximately the same but due to the initial time required for the recycling of the activated sludge, this method took slightly longer. From an initial start-up loading of 0.486 kg m-3, d-1 (SS) and 0.568 kg m-3 d-1 (sCOD) suspended solids and soluble chemical oxygen demand removal efficiencies dropped to below 50 when loadings of 1.397 kg m-3 d-1 (SS) and 1.403 kg m-3, d-1 (sCOD) were reached. The floating media performed better at the higher flowrates under shock loading conditions th
机译:曝气生物滤池(BAF)在一个浸入式曝气三相反应器中结合了生物处理和固体去除功能。在过去的20年中,生物充气滤池不仅作为滴滤池和活性污泥厂等其他二级处理系统的竞争对手,而且还作为三级处理系统而开发。这项工作的目的是比较两个这样的反应堆的性能,一个反应堆在启动期间和增加的水力流量下,在相同的条件下,一个反应堆包含一个浮动介质,另一个反应堆包含一个沉没的介质。使用了两种启动方法。第一种方法使用活性污泥作为种子,将其循环通过反应器,第二种方法涉及简单地使工艺液体(沉降的生活污水)以初始流量通过反应器。经过一段时间的稳态后,流量逐渐增加,并且在每次增加期间和之后都对反应堆的性能进行了分析。启动的结果表明,使用这两种方法达到稳态的总时间大致相同,但由于回收活性污泥需要初始时间,因此该方法花费的时间略长。从最初的启动负荷0.486 kg m-3,d-1(SS)和0.568 kg m-3 d-1(sCOD)悬浮固体和可溶性化学需氧量去除效率在负荷为1.397 kg时降至50以下达到m-3 d-1(SS)和1.403 kg m-3,d-1(sCOD)。在冲击载荷条件下,浮动介质在较高流量下表现更好

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