首页> 外文期刊>International journal of green energy >THE BIOHYDROGEN POTENTIAL OF DISTILLERY WASTEWATER BY DARK FERMENTATION IN AN ANAEROBIC SEQUENCING BATCH REACTOR
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THE BIOHYDROGEN POTENTIAL OF DISTILLERY WASTEWATER BY DARK FERMENTATION IN AN ANAEROBIC SEQUENCING BATCH REACTOR

机译:厌氧间歇式反应器发酵发酵产生的废水中氢势。

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Potential of biohydrogen production from distillery wastewater was studied by dark fermentation in an anaerobic sequencing batch reactor. The active volume of the reactor was 3.5 L. Anaerobic distillery sludge subjected to acid, chemical and heat-shock pre-treatment was used as inoculum. The reactor was operated at ambient temperature under dark condition with three cycles per day. Each cycle of operation consisted of four sequential steps: feed, react, settle and decant. The organic loading rate was increased by decreasing the hydraulic retention time from 96 to 72, 48, 36, and 24 h. Gas production trend and cumulative gas production were studied at various hydraulic retention times. The substrate degradation rate was found to vary from 12.65 to 23.52 kg_(COD)/m~3/d at organic loading rates of 24 and 96 kg_(COD)/m~3 /d respectively. Experimental data showed the feasibility of biogas production along with substrate degradation with distillery wastewater as substrate.
机译:通过在厌氧测序间歇反应器中进行暗发酵研究了酿酒厂废水中生物氢的生产潜力。反应器的活性体积为3.5L。使用经过酸,化学和热冲击预处理的厌氧蒸馏厂污泥作为接种物。该反应器在环境温度,黑暗条件下每天操作三个循环。每个操作周期包括四个连续步骤:进料,反应,沉降和倾析。通过将水力停留时间从96小时减少到72、48、36和24小时,可以增加有机负荷率。研究了在不同水力停留时间下的产气趋势和累计产气量。发现在有机负载量分别为24和96 kg_(COD)/ m〜3 / d的情况下,底物降解速率在12.65至23.52 kg_(COD)/ m〜3 / d之间变化。实验数据表明,以酿酒厂废水为底物,沼气生产以及底物降解的可行性。

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