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Treatment of petroleum refinery wastewater using a sequential anaerobic-aerobic moving-bed biofilm reactor system based on suspended ceramsite

机译:基于悬浮陶粒的顺序厌氧-好氧移动床生物膜反应器系统处理炼油厂废水

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In this study, a novel suspended ceramsite was prepared, which has high strength, optimum density (close to water), and high porosity. The ceramsite was used to feed a moving-bed biofilm reactor (MBBR) system with an anaerobic-aerobic (A/O) arrangement to treat petroleum refinery wastewater for simultaneous removal of chemical oxygen demand (COD) and ammonium. The hydraulic retention time (HRT) of the anaerobic-aerobic MBBR system was varied from 72 to 18 h. The anaerobic-aerobic system had a strong tolerance to shock loading. Compared with the professional emission standard of China, the effluent concentrations of COD and NH_3-N in the system could satisfy grade I at HRTs of 72 and 36 h, and grade II at HRT of 18 h. The average sludge yield of the anaerobic reactor was estimated to be 0.0575 g suspended solid/g COD _(removed). This work demonstrated that the anaerobic-aerobic MBBR system using the suspended ceramsite as biocarrier could be applied to achieving high wastewater treatment efficiency.
机译:在这项研究中,制备了一种新型的悬浮陶粒,该陶粒具有高强度,最佳密度(接近水)和高孔隙率。陶粒用于给具有厌氧-好氧(A / O)装置的移动床生物膜反应器(MBBR)系统进料,以处理炼油厂废水,同时去除化学需氧量(COD)和铵。厌氧-好氧MBBR系统的水力停留时间(HRT)从72到18 h不等。厌氧-好氧系统对冲击负荷具有很强的耐受性。与中国的专业排放标准相比,系统中COD和NH_3-N的废水浓度在HRT分别为72和36 h时达到I级,在HRT为18 h时达到II级。厌氧反应器的平均污泥产率估计为0.0575 g悬浮固体/ g COD_(去除)。这项工作表明,以悬浮的陶粒为生物载体的厌氧-好氧MBBR系统可用于实现高废水处理效率。

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