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Performance of simultaneous organic and nutrient removal in a pilot scale anaerobic-anoxic-oxic membrane bioreactor system treating municipal wastewater with a high nutrient mass ratio

机译:中试规模厌氧-缺氧-氧膜生物反应器系统同时去除有机物和养分的性能以高养分质量比处理市政废水

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A pilot-scale anaerobic-anoxic-oxic membrane bioreactor (A2O-MBR) was applied to treat Shiraz municipal wastewater with high ratio of total phosphorous (TP): total nitrogen (TN): chemical oxygen demand (COD) (3.4: 21.4: 100) and remarkable nitrate concentration. Various operating conditions were tested to investigate nutrient and organic matter removal as well as membrane capacity and biomass development. The pilot system was operated at a constant sludge retention time of 60 d. During different runs, the biomass concentration increased with a reduction of HRT while the F/M ratio was stable around an average of 0.087 gCOD g(-1)MLSS d(-1). Results also showed that the treatment performance of A2O-MBR system was extremely stable and was not affected by aerobic hydraulic retention time (HRT) changes (12, 10, 8, 6 h). COD reduction reached over 95% and nitrification was completed. The maximum efficiency of TN and TP removal was 86.2% and 55.9%, respectively, which occurred with an overall HRT of 12 h, external and internal mixed liquor recycle rate of 200%. Membrane capacity measurements showed an average flux of 5.5 L m(-2) h(-1) with a mean transmembrane pressure of 30 kPa under periodical air backwashing without any chemical cleaning over three months. (C) 2015 Elsevier Ltd. All rights reserved.
机译:中试规模的厌氧-缺氧-氧化膜生物反应器(A2O-MBR)用于处理设拉子的城市废水,其总磷(TP):总氮(TN):化学需氧量(COD)的比例高(3.4:21.4: 100)和明显的硝酸盐浓度。测试了各种操作条件以研究营养和有机物的去除以及膜的容量和生物量的发育。中试系统在60 d的恒定污泥保留时间下运行。在不同的运行过程中,生物量浓度随HRT的降低而增加,而F / M比稳定在平均0.087 gCOD g(-1)MLSS d(-1)附近。结果还表明,A2O-MBR系统的处理性能非常稳定,不受有氧水力停留时间(HRT)变化(12、10、8、6 h)的影响。化学需氧量减少达到95%以上,硝化作用完成。 TN和TP去除的最大效率分别为86.2%和55.9%,这发生在总HRT为12 h,内部和外部混合液再循环率为200%的情况下。膜容量测量显示,在三个月内不进行任何化学清洗的情况下,定期进行空气反冲洗后,平均通量为5.5 L m(-2)h(-1),平均跨膜压力为30 kPa。 (C)2015 Elsevier Ltd.保留所有权利。

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