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Post-treatment of UASB effluent in an expanded granular sludge bed reactor type using flocculent sludge

机译:使用絮凝污泥对膨胀型颗粒污泥床反应器类型中的UASB废水进行后处理

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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 (V-up). 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 V-up 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. [References: 10]
机译:评估了使用絮凝污泥的EGSB(膨胀颗粒污泥床)反应器类型对UASB反应器处理生活污水的后处理性能。在331天的时间内对中试规模的157.5-L EGSB反应器进行了监测。 EGSB反应器的最初概念是基于颗粒污泥的使用和高流速液体(V-up)的应用。但是,即使使用UASB规模的絮凝污泥(巴西累西腓的Mangueira工厂),也可以实现良好的混合条件和高生物质保留率。通过应用4小时的水力停留时间和高达3.75 m / h的V-up值,EGSB中的总化学和过滤后样品的化学需氧量浓度分别低于87 mg / L和55 mg / L。废水中总悬浮固体(TSS)浓度低于32 mg / L。在整个实验期间观察到良好的性能和稳定的反应器操作。因此,使用絮凝污泥的EGSB反应器类型还可用于后处理来自生活污水的反应器中的非常稀的厌氧废水的后处理。 [参考:10]

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