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Anaerobic treatment of low-strength wastewater: A comparison between single and staged anaerobic fluidized bed membrane bioreactors

机译:低强度废水的厌氧处理:单阶段厌氧流化床膜生物反应器的比较

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摘要

Performance of a single anaerobic fluidized membrane bioreactor (AFMBR) was compared with that of a staged anaerobic fluidized membrane bioreactor system (SAF-MBR) that consisted of an anaerobic fluidized bed bioreactor (AFBR) followed by an AFMBR. Both systems were fed with an equal COD mixture (200 mg/L) of acetate and propionate at 25 ℃. COD removals of 93–96% were obtained by both systems, independent of the hydraulic retention times (HRT) of 2–4 h. Over more than 200 d of continuous operation, trans-membrane pressure (TMP) in both systems was less than 0.2 bar without significant membrane fouling as a result of the scouring of membrane surfaces by the moving granular activated carbon particles. Results of bulk liquid suspended solids, extracellular polymeric substances (EPS), and soluble microbial products (SMP) analyses also revealed no significant differences between the two systems, indicating the single AFMBR is an effective alternative to the SAF-MBR system.
机译:将单个厌氧流化膜生物反应器(AFMBR)的性能与分段厌氧流化膜生物反应器系统(SAF-MBR)的性能进行了比较,该系统由厌氧流化床生物反应器(AFBR)和AFMBR组成。在25℃下,向两个系统中均加入乙酸和丙酸酯的等量COD混合物(200 mg / L)。两种系统均可实现93–96%的COD去除,而与2-4 h的水力停留时间(HRT)无关。在超过200 d的连续运行过程中,两个系统中的跨膜压力(TMP)均小于0.2 bar,并且由于移动的颗粒状活性炭颗粒对膜表面的冲刷而没有明显的膜污染。散装液体悬浮固体,细胞外聚合物(EPS)和可溶性微生物产品(SMP)的分析结果还显示,这两个系统之间没有显着差异,表明单个AFMBR是SAF-MBR系统的有效替代品。

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