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Mixed pharmaceutical wastewater treatment by integrated membrane-aerated biofilm reactor (MABR) system - A pilot-scale study

机译:集成膜曝气生物膜反应器(MABR)系统处理混合制药废水-中试研究

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摘要

A pilot-scale integrated membrane-aerated biofilm reactor (MABR) system, consisted of hydrolysis/acidification pretreatment, MABR process and activated carbon adsorption post-processing, was designed to treat the high-loading mixed pharmaceutical wastewater. A study of MABR process was conducted to investigate the effect of aeration condition, circulation flow rate and water quality on performance over 260days. The performances of these processes were evaluated by the removal efficiency of COD, BOD _5, turbidity, NH _4 ~+-N and TN. MABR process could effectively remove above 90% of COD and 98% of ammonia. The capacities per unit volume of MABR could reach up to 1311gCOD/m 3d and 48.2gNH _4 ~+-N/m ~3d with single membrane aeration, and the oxygen utilization rate could be as high as 45%. After post-processing, the effluent of integrated treatment MABR system kept stable with COD below 200mg/L and NH _4 ~+-N below 3mg/L.
机译:设计了由水解/酸化预处理,MABR工艺和活性炭吸附后处理组成的中试规模的膜曝气生物膜反应器(MABR)系统,用于处理高负荷混合制药废水。进行了MABR工艺研究,以研究曝气条件,循环流量和水质对260天性能的影响。通过去除COD,BOD_5,浊度,NH_4〜+ -N和TN的去除效率来评估这些工艺的性能。 MABR工艺可以有效去除90%以上的COD和98%的氨。单膜曝气MABR的单位体积容量可达到1311gCOD / m 3d和48.2gNH_4〜+ -N / m〜3d,氧利用率可达45%。后处理后,综合处理的MABR系统的废水保持稳定,COD低于200mg / L,NH _4〜+ -N低于3mg / L。

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