Jupsin H, Vasel J L
University of Liege, Département Sciences et Gestion de l'Environnement, Unité Assainissement et Environnement, 185 Avenue de Longwy, 6700 Arlon, Belgium.
Water Sci Technol. 2007;55(11):21-7. doi: 10.2166/wst.2007.341.
In aerated lagoons and even more in stabilization ponds the specific power (W/m3) is not high enough to maintain all the suspended solids in suspension. Some part of the suspended solids (including biomass) settles directly into the reactor and not in the final settling pond. The gradual accumulation of those sediments on the pond bottom affects performance by reducing the pond volume and shortening the Hydraulic Residence Time. However, the role played by these deposits is not restricted to such a physical effect. Far from being inert sediments they are also an important oxygen sink that must be taken into account when designing aerator power and oxygen supply, for example. On the other hand, under aerobic conditions, the upper layer of sediments may contribute to the treatment as a biofilm compartment in the reactor. In aerated lagoon systems another process contributes to the interaction of deposits and the liquid phase: the operating (often sequencing) of aerators may induce a drastic resuspension of deposits. In a 3,000 m3 aerated lagoon we evaluated that 3 tons of deposits were resuspended when aerators were started. Due to those processes we consider that a mathematical model of an aerated lagoon or of a stabilization pond has to take into account the contribution (positive and negative aspects) of deposits in the process. In this paper we propose a model for sediments including production but also biological processes. Simulations of the aerated lagoon with or without the "sediment compartment" demonstrate the effect and the importance of this compartment on the process. Of course a similar approach could be used for facultative or even maturation ponds. The next step would be to include anaerobic activities in the bottom layer.
在曝气塘中,甚至在稳定塘中,单位功率(瓦/立方米)不足以使所有悬浮固体保持悬浮状态。部分悬浮固体(包括生物质)直接沉降到反应器中,而不是在最终沉淀池。这些沉积物在池底的逐渐积累会通过减小池塘容积和缩短水力停留时间来影响其性能。然而,这些沉积物所起的作用并不局限于这种物理效应。它们远非惰性沉积物,还是一个重要的氧汇,例如在设计曝气器功率和氧气供应时必须加以考虑。另一方面,在有氧条件下,沉积物的上层可能作为反应器中的生物膜隔室对处理过程有所贡献。在曝气塘系统中,另一个过程导致沉积物与液相相互作用:曝气器的运行(通常是顺序运行)可能会引起沉积物的剧烈再悬浮。在一个3000立方米的曝气塘中,我们评估出曝气器启动时会有3吨沉积物被再悬浮。由于这些过程,我们认为曝气塘或稳定塘的数学模型必须考虑沉积物在该过程中的作用(积极和消极方面)。在本文中,我们提出了一个包含沉积物产生及生物过程的模型。对有或没有“沉积物隔室”的曝气塘进行模拟,证明了该隔室对过程的影响及重要性。当然,类似的方法也可用于兼性塘甚至熟化塘。下一步将是纳入底层的厌氧活动。