Kato M T, Florencio L, Arantes R F M
Federal University of Pernambuco, Department of Civil Engineering, Av. Acadêmico Hélio Ramos s/n, Cidade Universitaria, 50740-530 Recife, Pernambuco, Brazil.
Water Sci Technol. 2003;48(6):279-84.
The performance of an EGSB (expanded granular sludge bed) reactor type using flocculent sludge was evaluated for the post-treatment of effluent from UASB reactor treating domestic sewage. A pilot-scale 157.5-L EGSB reactor was monitored during a 331-day period. The original concept of the EGSB reactor was based on granular sludge use and by applying of high upflow liquid velocities (Vup). However, even using flocculent sludge from a UASB full-scale (Mangueira Plant, Recife, Brazil), good mixing conditions and high retention of biomass were achieved. By applying a 4-h hydraulic retention time and Vup values up to 3.75 m/h, effluent chemical oxygen demand concentrations in the EGSB were below 87 mg/L and 55 mg/L, for total and filtered samples, respectively. Total suspended solid (TSS) concentrations in the effluent were below 32 mg/L. Good performance and stable reactor operation during the whole experimental period were observed. Therefore, the EGSB reactor type using flocculent sludge can also be used for post-treatment of very dilute anaerobic effluent from reactors treating domestic sewage.
对使用絮凝污泥的膨胀颗粒污泥床(EGSB)反应器类型处理生活污水的上流式厌氧污泥床(UASB)反应器出水进行后处理效果进行了评估。在331天的时间内对一个中试规模的157.5升EGSB反应器进行了监测。EGSB反应器的最初概念基于使用颗粒污泥并采用较高的上流液体流速(Vup)。然而,即使使用来自巴西累西腓Mangueira工厂全尺寸UASB的絮凝污泥,也实现了良好的混合条件和较高的生物量保留率。通过采用4小时的水力停留时间和高达3.75米/小时的Vup值,EGSB中总样品和过滤样品的出水化学需氧量浓度分别低于87毫克/升和55毫克/升。出水中的总悬浮固体(TSS)浓度低于32毫克/升。在整个实验期间观察到了良好的性能和稳定的反应器运行。因此,使用絮凝污泥的EGSB反应器类型也可用于处理生活污水的反应器产生的极稀厌氧出水的后处理。