Su Y C, Huang C P, Pan Jill R, Lee H C
Institute of Environmental Engineering, National Chiao Tung University, 75 Po-Ai Street, Hsinchu, Chinese Taiwan.
Water Sci Technol. 2008;57(4):601-5. doi: 10.2166/wst.2008.111.
Recently, the membrane bioreactor (MBR) process has become one of the novel technologies to enhance the performance of biological treatment of wastewater. Membrane bioreactor process uses the membrane unit to replace a sediment tank, and this can greatly enhance treatment performance. However, membrane fouling in MBR restricts its widespread application because it leads to permeate flux decline, making more frequent membrane cleaning and replacement necessary, which then increases operating and maintenance costs. This study investigated the sludge characteristics in membrane fouling under sub-critical flux operation and also assessed the effect of shear stress on membrane fouling. Membrane fouling was slow under sub-critical flux operation. However, as filamentous microbes became dominant in the reactor, membrane fouling increased dramatically due to the increased viscosity and polysaccharides. A close link was found between membrane fouling and the amount of polysaccharides in soluble EPS. The predominant resistance was the cake resistance which could be minimized by increasing the shear stress. However, the resistance of colloids and solutes was not apparently reduced by increasing shear stress. Therefore, smaller particles such as macromolecules (e.g. polysaccharides) may play an important role in membrane fouling under sub-critical flux operation.
近年来,膜生物反应器(MBR)工艺已成为提高废水生物处理性能的新技术之一。膜生物反应器工艺使用膜单元取代沉淀池,这可大大提高处理性能。然而,MBR中的膜污染限制了其广泛应用,因为它会导致渗透通量下降,使得更频繁地进行膜清洗和更换成为必要,进而增加了运行和维护成本。本研究调查了亚临界通量运行下膜污染中的污泥特性,并评估了剪切应力对膜污染的影响。在亚临界通量运行下,膜污染进展缓慢。然而,随着丝状微生物在反应器中占主导地位,由于粘度和多糖增加,膜污染急剧增加。发现膜污染与可溶性胞外聚合物(EPS)中多糖的量之间存在密切联系。主要阻力是滤饼阻力,可通过增加剪切应力将其降至最低。然而,增加剪切应力并未明显降低胶体和溶质的阻力。因此,较小的颗粒如大分子(如多糖)可能在亚临界通量运行下的膜污染中起重要作用。