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An approach to enhance permeate flux of submerged ultra-filtration membrane system

机译:一种提高浸没式超滤膜系统渗透通量的方法

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Total experimental period was divided into two stages. At the first stage, two runs of experiments were carried out to obtain an understanding of the effect of activated sludge concentration and SCOD in membrane bioreactor (MBR) on ultra-filtration (UF) membrane permeate flux. It was found that in a reactor with an excellent biological treatment performance, the majority of the increasing resistance was attributed to cake resistance; while in an environment with high organics, the fouling resistance increased at a rate higher than the cake resistance did. On the basis of experimental investigations, a concept of "protection coating layer" was proposed to illustrate the phenomenon of UF membrane fouling. At the second experimental stage, powdered activated carbon (PAC) was applied to the test reactor to enhance the formation of "protection coating layer". During the operational period of 32 days, compared with the control system, test system obtained higher removals for COD, NH_3-N, TN and TP by 1.15%, 1.39%, 6.75% and 8.3% respectively, and fouling rate of the UF membrane in it was also alleviated.
机译:实验总时间分为两个阶段。在第一阶段,进行了两次实验,以了解膜生物反应器(MBR)中活性污泥浓度和SCOD对超滤(UF)膜渗透通量的影响。发现在具有优异生物处理性能的反应器中,大部分增加的阻力归因于抗滤饼性。而在有机物含量较高的环境中,耐污垢性的提高速度要高于抗滤饼性。在实验研究的基础上,提出了“保护涂层”的概念来说明超滤膜结垢现象。在第二个实验阶段,将粉末状活性炭(PAC)应用于测试反应器,以增强“保护涂层”的形成。在运行的32天中,与对照系统相比,测试系统对COD,NH_3-N,TN和TP的去除率分别提高了1.15%,1.39%,6.75%和8.3%,并且超滤膜的结垢率更高在其中也得到缓解。

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