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A comparison of a blower and a Venturi aeration system in a submerged membrane bioreactor

机译:潜水膜生物反应器中鼓风机和文丘里曝气系统的比较

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A novel aeration method for submerged membrane bioreactors (MBR) was developed in this study. This method uses a Venturi injector to supply the air to the MBR. Short term experiments were performed to determine the technical applicability of integrating a venturi device into a submerged MBR. A flat-sheet, 0.1-mu m polyvinylidene fluoride membrane was used to operate the MBR. Real wastewater taken from Diyarbakir Municipal Wastewater Treatment Plant was used as feed. Membrane fouling was evaluated under three different fluxes (18, 32, and 50 L/m(2) . h) and 3 L/min aeration rate for both blower-and venturi-aerated MBR systems. Transmembrane pressure (TMP), chemical oxygen demand (COD), mixed liquor suspended solids, mixed liquor volatile suspended solids, pH, dissolved oxygen, and temperature were measured in the experimental setup. The COD removal rate was between 75-92% for blower system and 85-87% for venturi system. Effluent NH4-N concentration was between 0.0-14.7 mg/L for blower system and 0.0-0.7 for venturi system. While the effluent NO3-N was between 3.1-27.4 mg/L for blower system, it was 33.3-37.8 mg/L for venturi system. At 3 L/min aeration rate, the dissolved oxygen concentration in MBR was between 0.42-3.43 mg/L for blower-aerated system and between 6.43-7.07 mg/L for venturi-aerated system. TMP development at different fluxes in blower and venturi systems showed that integration of a venturi device with a submerged MBR improved filtration capacity significantly. The rate of TMP increase in blower-aerated system was higher than that of venturi-aerated system at the same aeration rate of 3 L/min for both systems. At the highest filtration flux tested (50 L/m(2) . h), venturi-aerated system operated three times longer than the blower system.
机译:在这项研究中开发了一种新的曝气膜生物反应器(MBR)的方法。该方法使用文丘里喷射器将空气供应到MBR。进行了短期实验,以确定将文丘里管装置集成到水下MBR中的技术适用性。使用平板式0.1微米聚偏二氟乙烯膜操作MBR。取自迪亚巴克尔市政废水处理厂的实际废水用作饲料。在鼓风机和文丘里通气的MBR系统的三种不同通量(18、32和50 L / m(2).h)和3 L / min的曝气速率下,对膜污染进行了评估。在实验装置中测量跨膜压力(TMP),化学需氧量(COD),混合液悬浮固体,混合液挥发性悬浮固体,pH,溶解氧和温度。鼓风机系统的COD去除率在75-92%之间,文丘里系统的COD去除率在85-87%之间。鼓风机系统出水NH4-N浓度在0.0-14.7 mg / L之间,文丘里系统出水在0.0-0.7之间。鼓风机系统的出水NO3-N在3.1-27.4 mg / L之间,文丘里系统的出水NO3-N在33.3-37.8 mg / L之间。在3 L / min的曝气速率下,鼓风机充气系统的MBR中溶解氧浓度在0.42-3.43 mg / L之间,而文丘里充气系统的溶解氧浓度在6.43-7.07 mg / L之间。在鼓风机和文丘里管系统中以不同通量进行的TMP开发表明,文丘里管装置与浸没式MBR的集成可显着提高过滤能力。在相同的3 L / min曝气速率下,两个系统的鼓风机充气系统中TMP的增加速度均高于文丘里充气系统。在测试的最高过滤通量(50 L / m(2)。h)下,文丘里通风系统的运行时间比鼓风机系统长三倍。

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