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Enhancement of the anaerobic hydrolysis and fermentation of municipal solid waste in leachbed reactors by varying flow direction during water addition and leachate recycle

机译:通过在加水和沥滤液循环过程中改变流向来增强沥滤床反应器中城市固体废物的厌氧水解和发酵

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Poor performance of leachbed reactors (LBRs) is attributed to channelling, compaction from waste loading, unidirectional water addition and leachate flow causing reduced hydraulic conductivity and leachate flow blockage. Performance enhancement was evaluated in three LBRs M, D and U at 22 ± 3 ℃ using three water addition and leachate recycle strategies; water addition was downflow in D throughout, intermittently upflow and downflow in M and U with 77% volume downflow in M, 54% volume downflow in U while the rest were upflow. Leachate recycle was downflow in D, alternately downflow and upflow in M and upflow in U. The strategy adopted in U led to more water addition (30.3%), leachate production (33%) and chemical oxygen demand (COD) solubilisation (33%; 1609 g against 1210 g) compared to D (control). The total and volatile solids (TS and VS) reductions were similar but the highest COD yield (g-COD/g-TS and g-COD/g-VS removed) was in U (1.6 and 1.9); the values were 1.33 and 1.57 for M, and 1.18 and 1.41 for D respectively. The strategy adopted in U showed superior performance with more COD and leachate production compared to reactors M and D.
机译:浸出床反应器(LBR)的性能差归因于窜流,废物装载造成的压实,单向加水和浸出液流动,从而导致水力传导率降低和浸出液流动受阻。使用三种加水和渗滤液循环策略,在22±3℃的三个LBR M,D和U中评估了性能增强;整个过程中,水的添加是D中的下降,M和U中的上升和下降是间歇性的,M中的体积下降为77%,U中的体积下降为54%,其余部分为上升。渗滤液循环是D的下降,M的上升和下降以及U的上升。U中采用的策略导致更多的水添加(30.3%),渗滤液产生(33%)和化学需氧量(COD)增溶(33%) ;相对于D(对照),是1609 g,而1210 g)。总固体和挥发性固体(TS和VS)的减少量相似,但最高的COD产量(g-COD / g-TS和g-COD / g-VS去除量)以U为单位(1.6和1.9)。 M的值分别为1.33和1.57,D的值分别为1.18和1.41。与反应器M和D相比,U中采用的策略显示出更高的性能,产生了更多的COD和渗滤液。

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