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Feasibility of the UASB/AF system for domestic sewage treatment in developing countries

机译:UASB / AF系统在发展中国家生活污水处理中的可行性

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This paper presents the results of three pilot units comprising one UASB reactor followed by two anaerobic filters (AFs) operating in parallel (upflow and downflow modes). The UASB reactor had a volume of 416 litres, being operated at hydraulic retention times (HRT) of 6 and 4 hours. The anaerobic filters had total volumes of 102 litres (32 litres of packing material), being operated at HRT varying from 24 to 1.5 hours (upflow velocities varying from 0.06 to 1.44 mm). These different operational conditions characterised seven phases of research. Both reactors were fed with domestic sewage pumped directly from the main interceptor of Belo Horizonte city - Brazil. After almost one year of continuous monitoring, the UASB/AF system produced very good results in terms of COD and BOD removal, and also very low solids concentration in the final effluent. The average results of COD and BOD removal varied from 85 to 95%, sufficient to maintain the COD concentration in the final effluent in the range of 60 to 90 mg/l and the BOD values systematically below 40 mg/l. The overall averages of SS in the final effluent were kept below 25 mg/l. The UASB/AF system could become a very promising alternative for the treatment of domestic sewage in developing countries, since the system can be designed at very short hydraulic retention times (6 hours for the UASB reactor and 3 to 4 hours for the AF), resulting in a very compact and low cost treatment unit. Besides, there is no energy consumption and the labour costs are minimum. (C) 1998 IAWQ Published by Elsevier Science Ltd. All rights reserved. [References: 8]
机译:本文介绍了三个先导装置的结果,这些装置包括一个UASB反应器,然后是两个平行运行(上流和下流模式)的厌氧滤池(AF)。 UASB反应器的容量为416升,在6和4小时的水力停留时间(HRT)下运行。厌氧滤池的总体积为102升(32升填料),在HRT上运行的时间为24到1.5小时(上流速度在0.06到1.44 mm之间)。这些不同的运行条件表征了七个研究阶段。两个反应堆都装有直接从巴西贝洛哈里桑塔市的主要拦截器泵入的生活污水。经过近一年的连续监测,UASB / AF系统在去除COD和BOD方面产生了非常好的结果,并且最终废水中的固体浓度也非常低。 COD和BOD去除的平均结果在85%到95%之间变化,足以使最终废水中的COD浓度保持在60至90 mg / l的范围内,而BOD值系统地低于40 mg / l。最终废水中SS的总体平均值保持在25 mg / l以下。 UASB / AF系统可能会成为发展中国家处理生活污水的非常有前途的替代方法,因为该系统可以在很短的水力停留时间(UASB反应器为6小时,AF为3至4小时)设计,从而产生了非常紧凑且低成本的处理单元。此外,没有能源消耗,而且劳动力成本最低。 (C)1998年IAWQ,由Elsevier Science Ltd.出版。保留所有权利。 [参考:8]

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