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城市污水再生过程中膜生物反应器系统的性能研究

Performance investigation of membrane bioreactor systems during municipal wastewater reclamation.

作者信息

DeCarolis James F, Adham Samer

机构信息

MWH Americas Inc., 9444 Farnham Street, Suite 300, San Diego CA 92117, USA.

出版信息

Water Environ Res. 2007 Dec;79(13):2536-50. doi: 10.2175/106143007x212184.

DOI:10.2175/106143007x212184
PMID:18198699
Abstract

Four commercially available membrane bioreactor (MBR) systems were operated at the pilot scale, to investigate performance during the reclamation of municipal wastewater. The MBR performance was evaluated under a variety of operating conditions, including two types of feed wastewater (raw and advanced primary effluent), hydraulic retention times (HRTs) ranging from 2 to 6 hours, and permeate fluxes between 20 and 41 lmh. Test results showed that MBR systems were capable of operating on advanced primary effluent, despite the possible presence of coagulant and/or polymer residual, with minimal membrane fouling. Membrane performance data generated during this study was also used to quantify the relationship between permeate flux and membrane fouling. Cleaning intervals at various flux conditions were estimated as follows: 69 days at 20 lmh, 58 days at 25 lmh, and 30 days for operation between 31 and 41 lmh. It was also demonstrated that the MBR process could be optimized to operate with minimal fouling under high hydraulic (flux = 37 lmh) and organic loading (HRT = 2 hours and food-to-microorganism ratio = 0.33 g COD/g VSS x d) conditions. Water quality monitoring conducted throughout the study showed that each MBR system consistently produced an oxidized (5-day biochemical oxygen demand < 2 mg/L) and nitrified (ammonia < 1 mg-N/L) effluent low in particulate matter (turbidity < 0.1 NTU), under all conditions tested.

摘要

运行了四个市售的膜生物反应器(MBR)系统中试规模装置,以研究城市污水处理回用过程中的性能。在多种运行条件下对MBR性能进行了评估,包括两种类型的进水废水(原水和一级强化出水)、2至6小时的水力停留时间(HRT)以及20至41升/平方米·小时的渗透通量。测试结果表明,MBR系统能够处理一级强化出水,尽管可能存在混凝剂和/或聚合物残留,但膜污染最小。本研究期间生成的膜性能数据还用于量化渗透通量与膜污染之间的关系。不同通量条件下的清洗间隔估计如下:20升/平方米·小时时为69天,25升/平方米·小时时为58天,31至41升/平方米·小时运行时为30天。还证明了MBR工艺可以优化,以便在高水力(通量 = 37升/平方米·小时)和有机负荷(HRT = 2小时,食物-微生物比 = 0.33克化学需氧量/克挥发性悬浮固体×天)条件下以最小的污染运行。在整个研究过程中进行的水质监测表明,在所有测试条件下,每个MBR系统始终产生氧化的(五日生化需氧量<2毫克/升)和硝化的(氨<1毫克氮/升)、颗粒物含量低(浊度<0.1 NTU)的出水。

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