Influence of operational conditions on the performance of a mesh filter activated sludge process

被引:98
作者
Fuchs, W [1 ]
Resch, C [1 ]
Kernstock, M [1 ]
Mayer, M [1 ]
Schoeberl, P [1 ]
Braun, R [1 ]
机构
[1] IFA Tulln, Dept Environm Biotechnol, A-3430 Tulln, Austria
关键词
activated sludge; mesh filter; wastewater treatment; sludge floc; F/M ratio;
D O I
10.1016/j.watres.2004.12.001
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Recently, a new type of wastewater treatment system became the focus of scientific research, the mesh filter activated sludge system. It is a modification of the membrane bioreactor where a membrane filtration process serves to separate the sludge from the purified effluent. The difference is that a mesh filter is used instead of the membrane. Due to the much larger pore size of the mesh, the effluent is not of the same excellent quality as with membrane bioreactors. Nevertheless, it still resembles the quality of the now most widely used standard treatment system, where settling tanks are used to retain the activated sludge. At the same time, the new system features all the other advantages of membrane bioreactors including elevated sludge concentrations resulting in decreased volumina of basins and complete substitution of the settling tank. Therefore, this process presents a potential future alternative where a small footprint of the plant is required. However, so far only a few preliminary studies on this innovative process type have been done. In this paper, the effects of suspended solids concentration, flux rate as well as aeration rate on the effluent quality are discussed. Furthermore, the characteristic of the sludge floc was identified as a factor of vital importance. Therefore, another influencing parameter, the food to microorganism (F/M) ratio, which is known to have a significant effect on floc characteristics, was studied. The main result demonstrated that the process was very effective under most of the operation conditions. The suspended solids concentration in the effluent was below 12 mg l(-1), the average COD in the effluent was between 24 and 45 mg l(-1) and the BOD5 was lower than 5 mg l(-1). High flux rates of up to 1501 m(-2) h(-1) were also achieved. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:803 / 810
页数:8
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