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用于废水处理的厌氧流化床膜生物反应器。

Anaerobic fluidized bed membrane bioreactor for wastewater treatment.

机构信息

Department of Environmental Engineering, Inha University, Namgu, Incheon, Republic of Korea.

出版信息

Environ Sci Technol. 2011 Jan 15;45(2):576-81. doi: 10.1021/es1027103. Epub 2010 Dec 15.

DOI:10.1021/es1027103
PMID:21158433
Abstract

Anaerobic membrane bioreactors have potential for energy-efficient treatment of domestic and other wastewaters, membrane fouling being a major hurdle to application. It was found that fouling can be controlled if membranes are placed directly in contact with the granular activated carbon (GAC) in an anaerobic fluidized bed bioreactor (AFMBR) used here for post-treatment of effluent from another anaerobic reactor treating dilute wastewater. A 120-d continuous-feed evaluation was conducted using this two-stage anaerobic treatment system operated at 35 °C and fed a synthetic wastewater with chemical oxygen demand (COD) averaging 513 mg/L. The first-stage was a similar fluidized-bed bioreactor without membranes (AFBR), operated at 2.0-2.8 h hydraulic retention time (HRT), and was followed by the above AFMBR, operating at 2.2 h HRT. Successful membrane cleaning was practiced twice. After the second cleaning and membrane flux set at 10 L/m(2)/h, transmembrane pressure increased linearly from 0.075 to only 0.1 bar during the final 40 d of operation. COD removals were 88% and 87% in the respective reactors and 99% overall, with permeate COD of 7 ± 4 mg/L. Total energy required for fluidization for both reactors combined was 0.058 kWh/m(3), which could be satisfied by using only 30% of the gaseous methane energy produced. That of the AFMBR alone was 0.028 kWh/m(3), which is significantly less than reported for other submerged membrane bioreactors with gas sparging for fouling control.

摘要

厌氧膜生物反应器具有高效处理家庭和其他废水的潜力,而膜污染是应用的主要障碍。如果将膜直接放置在用于处理另一个处理稀废水的厌氧反应器的出水的厌氧流化床生物反应器(AFMBR)中的颗粒活性炭(GAC)中,则可以控制污染。使用这种两段式厌氧处理系统进行了 120 天的连续进料评估,该系统在 35°C 下运行,并使用平均化学需氧量(COD)为 513mg/L 的合成废水进料。第一阶段是一个没有膜的类似流化床生物反应器(AFBR),水力停留时间(HRT)为 2.0-2.8 h,然后是上述的 AFMBR,HRT 为 2.2 h。成功地进行了两次膜清洗。第二次清洗后,将膜通量设定为 10 L/m(2)/h,在最后 40 天的运行中,跨膜压力从 0.075 线性增加到仅 0.1 巴。在各自的反应器中,COD 去除率分别为 88%和 87%,总去除率为 99%,透过液 COD 为 7±4mg/L。两个反应器组合的流化所需的总能量为 0.058 kWh/m(3),仅使用产生的气态甲烷能量的 30%即可满足。AFMBR 的单独能量为 0.028 kWh/m(3),明显低于其他用于控制污染的带气体喷射的浸没式膜生物反应器的报告值。

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