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Two stage intermittent aeration membrane bioreactor for simultaneous organic, nitrogen and phosphorus removal

机译:两级间歇曝气膜生物反应器,可同时去除有机物,氮和磷

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A submerged membrane bioreactor (SMBR) was operated in 2-stage intermittent aeration for simultaneous removal of organic matter, nitrogen and phosphorus. The system consists of two reactors with a total volume of 0.27 m(3) (1st reactor 0.09 m(3) and 2nd 0.18 m(3)). Real domestic wastewater was used as influent to the system. Membrane used for this experiment was hollow fiber polyethylene membrane with pore size of 0.1 mu m and effective surface area, 4 m(2). The membrane was submerged in the 2nd reactor for suction type filtration. Experiment was carried out in two phases varying the time cycles of aeration and non-aeration. SRT was maintained at 25 days and HRT, 16 similar to 19 hours. MLSS concentration in the reactors was in the range of 2,700-3,400 mg/l. The MLSS internal recycling ratio was maintained at 100% of influent flow rate. When time cycles of aeration and non-aeration were set at 30/90 min and 60/60 min in reactor 1 and 2, the removal of BOD and COD was 98.3% and 95.6%, respectively A relatively low nitrogen and phosphorus removal was observed in this condition (73.6% as T-N and 46.6% as T-P). However, with 60/60 min intermittent aeration conditions for both reactors, the removal rate of nitrogen and phosphorus for two weeks steady state were enhanced to 91.6% as TN and 66% as TP, respectively. Further a high organic removal (98% BOD and 96.2% COD) was achieved too. In these conditions, the membrane of flux declined from 0.1 m/d to 0.08 m/d and suction filtration was at 10 similar to 12 kPa fora month long operation period. [References: 9]
机译:浸没式膜生物反应器(SMBR)在两阶段间歇曝气中运行,以同时去除有机物,氮和磷。该系统由两个总体积为0.27 m(3)的反应器组成(第一个反应器为0.09 m(3)和第二个反应器为0.18 m(3))。实际的生活废水用作该系统的进水。用于该实验的膜是中空纤维聚乙烯膜,其孔径为0.1μm,有效表面积为4 m(2)。将该膜浸没在第二反应器中以进行吸滤。实验分两个阶段进行,改变充气和不充气的时间周期。 SRT维持在25天,HRT维持在16天,与19小时相似。反应器中的MLSS浓度为2,700-3,400 mg / l。 MLSS内部回收率保持在进水流量的100%。当在反应器1和2中将通气和不通气的时间周期设置为30/90分钟和60/60分钟时,BOD和COD的去除率分别为98.3%和95.6%,观察到相对较低的氮和磷去除率在这种情况下(TN为73.6%,TP为46.6%)。但是,在两个反应器均采用60/60分钟的间歇曝气条件下,两周稳态下氮和磷的去除率分别以TN和TP分别提高至91.6%和66%。此外,还实现了较高的有机去除率(98%BOD和96.2%COD)。在这些条件下,通量膜从0.1 m / d下降至0.08 m / d,抽滤在类似于12 kPa的10处进行了长达一个月的运行时间。 [参考:9]

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