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Performance analysis of a pilot-scale membrane aerated biofilm reactor for the treatment of landfill leachate

机译:中规模曝气生物膜反应器处理垃圾渗滤液的性能分析

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A 60 L membrane aerated biofilm reactor (MABR) was successfully employed to treat landfill leachate, which contained very high concentrations of refractory chemical oxygen demand (COD) and ammonium. Air or pure oxygen was supplied to the bioreactor through polydimethyl siloxane hollow fibre membranes. Over a year of operation with an average hydraulic retention time of about 5 days, and influent ammonium concentrations ranging from 500 to 2500 mg/L, the MABR achieved 80-99% nitrification. Simultaneously, the influent COD concentrations which ranged from 1000 to 3000 mg/L were reduced by approximately 200-500 mg/L. Oxygen transfer rates as high as 35 g O-2/m(2)-day were achieved during the study. By operating at low gas flowrates, high oxygen transfer efficiencies were achieved without any negative impact on oxygen transfer rates. This suggested that the biofilm was not oxygen limited during this study. The very low gas flowrates and the low pressure losses required to move air through the membranes resulted in very high standard aeration efficiencies that exceeded 10 kg O-2/kW h. The results indicate that mixing energy far exceeded that required for aeration in this study. Our results suggest that with process optimisation, MABR technology offers a low energy option for effective leachate treatment. (C) 2015 Elsevier B.V. All rights reserved.
机译:60 L膜曝气生物膜反应器(MABR)已成功用于处理垃圾渗滤液,其中包含非常高浓度的难处理化学需氧量(COD)和铵。通过聚二甲基硅氧烷中空纤维膜将空气或纯氧供应至生物反应器。在一年的运行中,平均水力停留时间约为5天,进水铵浓度范围为500至2500 mg / L,MABR的硝化率为80-99%。同时,进水COD浓度从1000到3000 mg / L降低了约200-500 mg / L。在研究过程中,氧的传输速率高达35 g O-2 / m(2)-天。通过在低气体流量下运行,可以实现较高的氧气传输效率,而对氧气传输速率没有任何负面影响。这表明在这项研究中生物膜不受氧的限制。极低的气体流速和使空气流过膜所需的低压损失导致非常高的标准曝气效率,超过10 kg O-2 / kW h。结果表明,混合能远远超出了本研究中曝气所需的能量。我们的结果表明,通过工艺优化,MABR技术为有效的渗滤液处理提供了低能耗的选择。 (C)2015 Elsevier B.V.保留所有权利。

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