Effectiveness of Using Floating Drum Bio-Digester to Treat Domestic Sewage

K. Adeniran, K. Kareem
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Abstract

An anaerobic floating drum digester was used in treating domestic sewage. The volumetric capacity of the digester plant was estimated as 258.99 litres with a 250 litre-gas holder tank. The gas holder tank was fitted into the digester tank with a clearance of about 2cm to allow the former rise freely when biogas is generated in the digester tank. An inlet pipe was introduced for loading the wastes into the digester and an outlet pipe for dislodging, with an overflow pipe which indicates the maximum extent to which the digester could be filled. A gas valve was incorporated at the top of the dome-shaped gas holder to control the gas flow. With the aid of a thermocouple wire fitted into the digester and a multimetre, the temperature of the sewage was monitored at a succession of 4 hours for a hydraulic retention period of 42 days. Sewage was obtained from a freshly dug soak away and fed into the bio-digester through the inlet pipe. Physical, chemical and bacteriological analyses were carried out before and during digestion process on daily basis. Results show that Biochemical Oxygen Demand (BOD) of the sewage before and after treatment was 96.50 mg/l and 55.50 mg/l respectively. The Chemical Oxygen Demand (COD) was 81.60 mg/l and 59.00 mg/l, before and after treatment respectively. The dissolved oxygen (DO) reduced from 124.80 mg/l to 84.30mg/l after a hydraulic retention period of 42 days. These results of the resulting treated water agreed to a reasonable level with the standards slated in the World Health Organisation (WHO, 2006) standards for safe disposal of wastewater. Keywords : Anaerobic bio-digester, domestic sewage, dislodging, thermocouple.
浮鼓式沼气池处理生活污水的效果研究
采用厌氧浮鼓式沼气池处理生活污水。消化装置的容量估计为258.99公升,并设有一个250公升的储气罐。储气罐安装在沼气池内,间隙约2cm,使储气罐在沼气池内产生沼气时可以自由上升。引入了一根进水管,用于将废物装载到蒸煮池中,并引入了一根出水管,用于排出废物,并引入了一根溢流管,以指示蒸煮池可以填充的最大程度。在圆顶型气柜的顶部安装了一个气体阀来控制气体流量。利用安装在沼气池内的热电偶导线和万用表,连续4小时监测污水的温度,水力滞留期为42天。污水从新挖的浸泡池中获得,并通过进水管进入生物沼气池。每天在消化前和消化过程中进行物理、化学和细菌学分析。结果表明,处理前后污水的生化需氧量(BOD)分别为96.50 mg/l和55.50 mg/l。处理前后的化学需氧量(COD)分别为81.60 mg/l和59.00 mg/l。在42天的水力滞留期后,溶解氧(DO)从124.80 mg/l降至84.30mg/l。经处理后的水的这些结果符合世界卫生组织(世卫组织,2006年)安全处理废水标准规定的合理水平。关键词:厌氧沼气池,生活污水,排水,热电偶
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