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采用厌氧/好氧混合侧流膜生物反应器处理造纸厂废水。

Treatment of paper mill effluent using an anaerobic/aerobic hybrid side-stream membrane bioreactor.

机构信息

Cape Peninsula University of Technology, Cape Town, South Africa.

出版信息

Water Sci Technol. 2012;65(7):1265-72. doi: 10.2166/wst.2012.007.

Abstract

This paper presents the design and operational performance data of an anaerobic/aerobic hybrid side-stream Membrane Bioreactor (MBR) process for treating paper mill effluent operated over a 6 month period. The paper mill effluent stream was characterized by a chemical oxygen demand (COD) range of between 1,600 and 4,400 mg/L and an average BOD of 2,400 mg/L. Despite large fluctuations in COD feed concentration, stable process performance was achieved. The anaerobic Expanded Granular Sludge Bed (EGSB) pre-treatment step effectively lowered the organic loading by 65 to 85%, thus lowering the MBR COD feed concentration to consistently below 750 mg/L. The overall MBR COD removal was consistent at an average of 96%, regardless of the effluent COD or changes in the hydraulic retention time (HRT) and organic loading rate (OLR). Combining a high-rate anaerobic pre-treatment EGSB with a Modified Ludzack-Ettinger (MLE) MBR process configuration produced a high quality permeate. Preliminary NF and RO results indicated an overall COD removal of around 97 and 98%, respectively.

摘要

本文介绍了一种用于处理造纸厂废水的厌氧/好氧混合侧流膜生物反应器(MBR)工艺的设计和运行性能数据,该工艺运行了 6 个月。造纸厂废水的化学需氧量(COD)范围为 1600 至 4400mg/L,平均生化需氧量(BOD)为 2400mg/L。尽管 COD 进料浓度波动较大,但仍实现了稳定的工艺性能。厌氧膨胀颗粒污泥床(EGSB)预处理步骤可将有机负荷降低 65%至 85%,从而将 MBR 的 COD 进料浓度稳定控制在 750mg/L 以下。无论出水 COD 如何变化,以及水力停留时间(HRT)和有机负荷率(OLR)如何变化,MBR 的 COD 去除率始终保持在 96%左右。将高负荷厌氧预处理 EGSB 与改良 Ludzack-Ettinger(MLE)MBR 工艺相结合,可产生高质量的渗透液。初步的纳滤(NF)和反渗透(RO)结果表明,COD 的总去除率分别约为 97%和 98%。

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