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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甲烷处理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 fornhydrogen and methane production. Neither physical nor chemical pre-treatments were used tonoptimize the process. The work was carried out at pilot scale, using two CSTRs (200 and 380 Lnworking volume respectively) both maintained at thermophilic temperature (55 WC) and fed semicontinuouslynwith biowaste. The experiment was divided into three periods; during the first twonperiods the organic loading rate was maintained at 20 kg TVS/m3 d and the hydraulic retention timenwas changed from 6.6 to 3.3 days, while in the last period the digestate of the second reactor wasnrecirculated to the first reactor in order to buffer the system and control pH at levels around 5. ThenHRT was maintained at 3.3 days and the OLR was decreased at 16.5 kg TVS/m3 d. The best yield wasnobtained in the last period where a specific hydrogen production of 50.9 L/kg VSfed was reached, withna H2 content in biogas from the first reactor of 36%. The methanogenic stage after the hydrogennconversion reached a specific biogas production of 0.62 m3/kg VSfed and an overall organic removalnabove 70%, without any stability problem. The overall biogas production was some 1.5 m3 per daynwith a gas composition of 10% H2 and 50% CH4.
机译:本文研究了处理生物废料氢和甲烷的两阶段厌氧工艺的优化。没有使用物理或化学预处理来优化工艺。该工作是在中试规模下进行的,使用了两个CSTR(分别为200和380 Ln工作容积),两个CSTR都保持在高温(55 WC)并半连续地注入生物废物。实验分为三个阶段。在最初的两个时期中,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,而在最后一个时期,第二个反应器的消化物不再循环到第一个反应器中,以缓冲系统并控制pH值在5左右。然后HRT维持在3.3天,OLR降低到16.5 kg TVS / m3 d。在最后一个时期没有获得最好的产量,在该期间达到了50.9 L / kg V​​Sfed的特定氢气产量,第一个反应器中沼气中的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,总体有机去除率在70%以上,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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