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A Bench Scale Study Of Fermentative Hydrogen And Methane Production From Food Waste In Integrated Two-stage Process

机译:综合两步法从食物垃圾中生产发酵性氢气和甲烷的基准规模研究

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A two-stage fermentation process combining hydrogen and methane production for the treatment of food waste was investigated in this paper. In hydrogen fermentation reactor, the indigenous mixed microbial cultures contained in food waste were used for hydrogen production. No foreign inoculum was used in the hydrogen fermentation stage, the traditional heat treatment of inoculum was not applied either in this bench scale experiment. The effects of the stepwise increased organic loading rate (OLR) and solid retention time (SRT) on integrated two-stage process were investigated. At steady state, the optimal OLR and SRT for the integrated two-stage process were found to be 22.65 kg VS/m~3 d (160 h) for hydrogen fermentation reactor and 4.61 (26.67 d) for methane fermentation reactor, respectively. Under the optimum conditions, the maximum yields of hydrogen (0.065 m~3H_2/kg VS) and methane (0.546 m~3 CH_4/kg VS) were achieved with the hydrogen and methane contents ranging from 29.42 to 30.86%, 64.33 to 71.48%, respectively. Biode-gradability analysis showed that 5.78% of the influent COD was converted to the hydrogen in H_2-SCRD and 82.18% of the influent COD was converted to the methane in CH_4-SCSTR under the optimum conditions.
机译:本文研究了氢气和甲烷生产相结合的两阶段发酵工艺,用于处理食物垃圾。在氢发酵反应器中,食物垃圾中所含的本地混合微生物培养物用于制氢。在氢发酵阶段不使用外来接种物,在该台式规模实验中也未应用传统的接种物热处理。研究了逐步增加的有机负荷率(OLR)和固体保留时间(SRT)对集成两步法的影响。在稳态下,对于氢气发酵反应器,集成两步法的最佳OLR和SRT分别为22.65 kg V​​S / m〜3 d(160 h),对于甲烷发酵反应器为4.61(26.67 d)。在最佳条件下,氢和甲烷含量分别为29.42〜30.86%,64.33〜71.48%,达到了最大产氢量(0.065 m〜3H_2 / kg V​​S)和甲烷(0.546 m〜3 CH_4 / kg V​​S)。 , 分别。生物降解性分析表明,在最佳条件下,H_2-SCRD中5.78%的进水COD转化为氢气,CH_4-SCSTR中82.8%的进水COD转化为甲烷。

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