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提取式生物膜膜生物反应器,可从过量曝气中回收能源,并控制新的膜污染。

Extractive biofilm membrane bioreactor with energy recovery from excess aeration and new membrane fouling control.

机构信息

Department of Chemical Engineering, King Mongkut's University of Technology Thonburi, Toongkru, Bangkok, Thailand.

出版信息

Bioresour Technol. 2011 Feb;102(3):2301-7. doi: 10.1016/j.biortech.2010.10.060. Epub 2010 Oct 20.

Abstract

Hybrid biofilm membrane bioreactor (BF-MBR) system featuring new mechanisms for recovering the excess energy from air bubbling flow in the biofilm reactor and for controlling membrane biofouling was preliminarily investigated in this study. Alternative design of the biofilm reactor was developed to utilize the bubbling flow from the lower aerobic chamber to generate a mechanical mixing in the upper anoxic chamber in the vertical biofilm reactor. Suspended solid (SS) concentration in the system was hydrodynamically controlled to be lower than 70 mg/L. The ultraviolet (UV) inactivation unit was integrated with the membrane filtration tank to limit biological activities for biofoulant productions and to decelerate the unwanted biofilm formation in the permeate tube. Membrane relaxations at various operating conditions were studied for optimum membrane fouling reductions under low SS environment. Combinations of membrane relaxation and the UV inactivation significantly prolonged sustainable operation periods of the membrane filtration in the BF-MBR process.

摘要

本研究初步探讨了一种具有新型机制的混合生物膜膜生物反应器 (BF-MBR) 系统,该系统可从生物膜反应器中的曝气流中回收多余能量,并控制膜生物污染。生物膜反应器的替代设计旨在利用下部好氧室的曝气流在上部缺氧室中产生机械混合,以在垂直生物膜反应器中实现。系统中的悬浮固体 (SS) 浓度通过水力学控制,使其低于 70mg/L。紫外线 (UV) 灭活单元与膜过滤槽集成在一起,以限制生物活性,防止生物污垢产生,并减缓渗透管中不需要的生物膜形成。在低 SS 环境下,研究了各种操作条件下的膜松弛,以实现最佳的膜污染减少。膜松弛和 UV 灭活的组合显著延长了 BF-MBR 工艺中膜过滤的可持续运行时间。

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