首页> 外文会议>The American Filtration and Separations Society presents: 9th world filtration congress >ANAEROBIC BIOREACTOR WITH IMMERSED MEMBRANE–PERFORMANCES AND MEMBRANE FOULING
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ANAEROBIC BIOREACTOR WITH IMMERSED MEMBRANE–PERFORMANCES AND MEMBRANE FOULING

机译:具有浸没膜性能的厌氧生物反应器和膜污染

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摘要

This study focuses on an anaerobic membrane bioreactor with an immersed membrane (IManBR) for wastewater treatment. Experiments were performed at lab scale with synthetic wastewater under psicrophilic conditions (temperature=20 °C) during 280 days. TOC and COD removals between 86 and 95% and between 87 and 90% were reached at organic loading rates of 1.5 kg COD/m~3.d. rnExperiments were performed using short filtration steps followed by long relaxation steps, and without backwashes. Some simple rinsing steps with pure water were also used and their efficiency to enhance the permeate flux was demonstrated. However a non-reversible fouling was also obtained, that can be characterized by an average loss of permeate flux obtained after rinsing of 0.09 l/m~2.h/d. rnThe influence of COD removal and accumulation of volatile fatty acids on the in-situ critical flux was studied. analysis of the dynamic comportment of the bioreactor after increases in organic loading rates allowed to establish a relationship between the critical flux and the concentration in volatile fatty acids (VFA), which is enhanced when the methanogenic activity is the limiting kinetic step of the biological process. This study points out that a good methanogenic activity is necessary to guaranty the removal of organic removal and also to limit membrane fouling.
机译:这项研究的重点是带有浸没膜(IManBR)的厌氧膜生物反应器,用于废水处理。实验是在实验室规模下用合成废水在高压条件下(温度= 20°C)进行的280天。有机负载量为1.5 kg COD / m〜3.d时,TOC和COD的去除率在86%至95%之间,在87%至90%之间。使用短的过滤步骤,然后进行长的松弛步骤,并且没有反洗,进行实验。还使用了一些简单的纯水冲洗步骤,并证明了它们提高渗透通量的效率。然而,还获得了不可逆的结垢,其特征在于漂洗后获得的渗透通量的平均损失为0.09 l / m〜2.h / d。 rn研究了COD的去除和挥发性脂肪酸的积累对原位临界通量的影响。对有机反应器增加负荷后生物反应器的动态比重进行分析,可以确定临界通量与挥发性脂肪酸(VFA)浓度之间的关系,而当产甲烷活性是生物过程的限制性动力学步骤时,这种关系会增强。这项研究指出,良好的产甲烷活性对于确保去除有机物以及限制膜污染是必要的。

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  • 会议地点 New Orleans LA(US);New Orleans LA(US)
  • 作者单位

    Centro de Investigaciones en Ingeniería Ambiental, Departamento de Ingeniería Civil y Ambiental,Universidad de los Andes, Carrera 65B No. 17A-11, Bogotá, Colombia,Laboratoire d’Ingénierie des Procédés de l’Environnement (LIPE), INSA Toulouse 135 Avenue de Rangueil, 31077 Toulouse Cedex 4, France;

    Centro de Investigaciones en Ingeniería Ambiental, Departamento de Ingeniería Civil y Ambiental,Universidad de los Andes, Carrera 65B No. 17A-11, Bogotá, Colombia;

    Centro de Investigaciones en Ingeniería Ambiental, Departamento de Ingeniería Civil y Ambiental,Universidad de los Andes, Carrera 65B No. 17A-11, Bogotá, Colombia;

    Laboratoire d’Ingénierie des Procédés de l’Environnement (LIPE), INSA Toulouse 135 Avenue de Rangueil, 31077 Toulouse Cedex 4, France;

    Laboratoire d’Ingénierie des Procédés d;

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