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Two-phase thermophilic anaerobic digestion process for biohythane production treating biowaste: Preliminary results

机译:两阶段高温厌氧消化工艺生产生物乙叉的生物废料的初步结果

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This paper deals with the optimization of a two-phase anaerobic process treating biowaste for hydrogen and methane production. Neither physical nor chemical pre-treatments were used to optimize the process. The work was carried out at pilot scale, using two CSTRs (200 and 380 L working volume respectively) both maintained at thermophilic temperature (55 °C) and fed semi-continuously with biowaste. The experiment was divided into three periods; during the first two periods the organic loading rate was maintained at 20 kg TVS/m3 d and the hydraulic retention time was changed from 6.6 to 3.3 days, while in the last period the digestate of the second reactor was recirculated to the first reactor in order to buffer the system and control pH at levels around 5. The HRT was maintained at 3.3 days and the OLR was decreased at 16.5 kg TVS/m3 d. The best yield was obtained in the last period where a specific hydrogen production of 50.9 L/kg VSfed was reached, with a H2 content in biogas from the first reactor of 36%. The methanogenic stage after the hydrogen conversion reached a specific biogas production of 0.62 m3/kg VSfed and an overall organic removal above 70%, without any stability problem. The overall biogas production was some 1.5 m3 per day with a gas composition of 10% H2 and 50% CH4.
机译:本文研究了处理生物废料用于生产氢气和甲烷的两阶段厌氧工艺的优化。物理或化学预处理均未用于优化工艺。该工作在中试规模下进行,使用两个CSTR(分别为200和380 L的工作体积),两个CSTR都保持在高温(55°C)下,并半连续地注入生物废物。实验分为三个阶段。在前两个阶段中,有机负荷率保持在20 kg TVS / m3 d,水力停留时间从6.6天更改为3.3天,而在最后阶段,第二反应器的消化物按顺序循环到第一反应器中缓冲系统并控制pH值在5左右。HRT保持在3.3天,OLR降低到16.5 kg TVS / m3 d。在最后一个时期获得了最佳产量,达到了50.9 L / kg V​​Sfed的特定氢气产量,第一反应器中沼气中的H2含量为36%。氢转化后的产甲烷阶段达到了0.62 m3 / kg V​​Sfed的特定沼气产量,总有机物去除率超过70%,而没有任何稳定性问题。每天的总沼气产量约为1.5 m3,气体成分为10%H2和50%CH4。

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