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Landfill leachate treatment using a rotating biological contactor and an upward-flow anaerobic sludge bed reactor

机译:使用旋转生物接触器和上流式厌氧污泥床反应器处理垃圾渗滤液

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This paper describes the feasibility of an aerobic system (rotating biological contactor, RBC) and a biological anaerobic system (upward-flow anaerobic sludge bed reactor) at small scale for the treatment of a landfill leachate. In the first phase of the aerobic system study, a cyclic-batch RBC system was used to select perforated acetate discs among three different acetate disc configurations. These discs were chosen on the basis of high COD removal (65%) and biological stability. In the second phase, the RBC system (using four stages) was operated continuously at different hydraulic retention times (HRT), at different rotational speeds, and with varying organic concentrations of the influent leachate (2500-9000 mg L~(-1)). Forty percent of the total surface area of each perforated disc was submerged in the leachate. A COD removal of about 52% was obtained at an HRT of 24 h and a rotational speed of 6 rpm. For the anaerobic system, the reactor was evaluated with a volumetric organic load of 3273 g-COD m~(-3) day~(-1) at an HRT of 54, 44, 39, 24 and 17 h. At these conditions, the system reached COD removal efficiencies of 62%, 61%, 59%, 44% and 24%, respectively.
机译:本文描述了一个小规模的好氧系统(旋转生物接触器,RBC)和生物厌氧系统(向上流厌氧污泥床反应器)用于处理垃圾渗滤液的可行性。在有氧系统研究的第一阶段,使用循环间歇式RBC系统从三种不同的乙酸酯盘配置中选择穿孔的乙酸酯盘。选择这些圆盘是基于高的COD去除率(65%)和生物稳定性。在第二阶段中,RBC系统(使用四个阶段)在不同的水力停留时间(HRT),不同的转速和不同的进水渗滤液有机浓度(2500-9000 mg L〜(-1))下连续运行)。每个多孔圆盘总表面积的40%浸没在渗滤液中。在24小时的HRT和6 rpm的转速下,COD去除率约为52%。对于厌氧系统,在HRT为54、44、39、24和17 h的条件下,以3273 g-COD m〜(-3)天〜(-1)的体积有机负荷评估反应器。在这些条件下,系统的COD去除效率分别为62%,61%,59%,44%和24%。

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