Non-woven fabric filter separation activated sludge reactor for domestic wastewater reclamation

A non-woven fabric filter was experimentally evaluated for solid-liquid separation in an activated sludge reactor as an alternative membrane. A polypropylene fabric filter (70, 50 and 35 g/m2) was used for the experiment. The pilot system was operated in A/O (Anaerobic/Oxic) type in which the filter...

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Veröffentlicht in:Water science and technology : a journal of the International Association on Water Pollution Research. - 1986. - 47(2003), 1 vom: 20., Seite 133-8
1. Verfasser: Seo, G T (VerfasserIn)
Weitere Verfasser: Moon, B H, Lee, T S, Lim, T J, Kim, I S
Format: Aufsatz
Sprache:English
Veröffentlicht: 2003
Zugriff auf das übergeordnete Werk:Water science and technology : a journal of the International Association on Water Pollution Research
Schlagworte:Journal Article Research Support, Non-U.S. Gov't Polypropylenes
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245 1 0 |a Non-woven fabric filter separation activated sludge reactor for domestic wastewater reclamation 
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520 |a A non-woven fabric filter was experimentally evaluated for solid-liquid separation in an activated sludge reactor as an alternative membrane. A polypropylene fabric filter (70, 50 and 35 g/m2) was used for the experiment. The pilot system was operated in A/O (Anaerobic/Oxic) type in which the filter module was submerged into the oxic compartment. The filtration module consists of 10 plate type rectangular filter elements with effective filtration area, 2 m2. Gravity filtration was carried out for solid-liquid separation by changing the water head 0.05-0.5 m without backwashing during the system operation. Initial permeate flux was set at 0.4 m/d. C/N ratio of raw wastewater was controlled at 4.5 in terms of BOD/T-N. The fabric filter system showed a good performance enough for domestic wastewater treatment. Effluent solid concentration was 3.2 mg/L (93.5% removal). COD removal efficiency was 91.6% producing an effluent concentration around 13 mg/L. 66% of total nitrogen removal could be obtained at the adjusted C/N ratio of influent wastewater. However phosphorus removal was very low at 23%. It was found that the initial flux of 0.4 m/d should be maintained for stable performance of the system 
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650 4 |a Research Support, Non-U.S. Gov't 
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700 1 |a Moon, B H  |e verfasserin  |4 aut 
700 1 |a Lee, T S  |e verfasserin  |4 aut 
700 1 |a Lim, T J  |e verfasserin  |4 aut 
700 1 |a Kim, I S  |e verfasserin  |4 aut 
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