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Cell wash-out enrichment increases the stability and performance of biohydrogen producing packed-bed reactors and the community transition along the operation time

机译:细胞洗提富集提高了生产生物氢的填充床反应器的稳定性和性能,并在运行时间内实现了社区过渡

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摘要

Most of the fermentative hydrogen production studies based on mixed cultures have shown enrichment of the microbial community by means of a heat treatment. This heat treatment enrichment strategy selects for Clostridum spp., an efficient hydrogen producer; however, other bacteria that may contribute to the systems performance could be excluded. Another enrichment strategy based on high dilution rates selects different taxonomic groups, which may affect hydrogen production and the system stability. In this work, two enrichment strategies were evaluated, heat shock and cell wash-out, for hydrogen production and the system stability in continuous stirred reactors. The enriched communities were then inoculated in packed bed reactors and operated up to 70 days. Both strategies selected hydrogen producing bacteria, mainly Clostridium spp. The highest hydrogen production rate (6.01 L H-2/L-d), molar yield (1.29 mol H-2/mol glucose(consumed)), and stability were achieved by the wash-out procedure; this high performance was attributed to facultative bacteria like Lactobacillus and Lactococcus. Furthermore, there was a transition within the community (along the operation time in the reactor with cell wash-out inoculum) and a selection for methanogenic activity (due to the long solids retention time). (C) 2016 Elsevier Ltd. All rights reserved.
机译:大多数基于混合培养物的发酵产氢研究表明,通过热处理可以丰富微生物群落。这种热处理富集策略选择了高效制氢剂梭菌属(Closridum spp。)。但是,可以排除可能影响系统性能的其他细菌。另一种基于高稀释率的富集策略选择了不同的生物分类群,这可能会影响氢气的产生和系统的稳定性。在这项工作中,针对连续搅拌反应器中的产氢和系统稳定性,评估了两种富集策略,即热激和细胞冲洗。然后将富集的群落接种在填充床反应器中,并运行长达70天。两种策略均选择产氢细菌,主要是梭状芽胞杆菌。通过冲洗程序可获得最高的产氢率(6.01 L H-2 / L-d),摩尔产率(1.29 mol H-2 / mol葡萄糖(已消耗))和稳定性。这种高性能归因于兼性细菌,如乳酸杆菌和乳球菌。此外,在群落内部有一个过渡(沿着反应器中带有细胞洗出接种物的操作时间)和产甲烷活性的选择(由于长的固体保留时间)。 (C)2016 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Renewable energy》 |2016年第11期|266-273|共8页
  • 作者单位

    Inst Potosino Invest Cient & Tecnol, Div Ciencias Ambientales, Camino Presa San Jose 2055,Lomas 4a Secc, San Luis Potosi 78216, SLP, Mexico|Univ Nacl Autonoma Mexico, Lab Res Adv Proc Water Treatment, Inst Ingn, Unidad Acad Juriquilla, Blvd Juriquilla 3001, Queretaro 76230, Mexico;

    Inst Potosino Invest Cient & Tecnol, Div Ciencias Ambientales, Camino Presa San Jose 2055,Lomas 4a Secc, San Luis Potosi 78216, SLP, Mexico|Univ Politecn Zacatecas, Plan Pardillo S-N,Parque Ind, Fresnillo 99059, Zac, Mexico;

    Inst Potosino Invest Cient & Tecnol, Div Ciencias Ambientales, Camino Presa San Jose 2055,Lomas 4a Secc, San Luis Potosi 78216, SLP, Mexico;

    Inst Potosino Invest Cient & Tecnol, Div Ciencias Ambientales, Camino Presa San Jose 2055,Lomas 4a Secc, San Luis Potosi 78216, SLP, Mexico;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Dark fermentation; Facultative bacteria; Heat treatment; Pretreatment;

    机译:黑暗发酵;细菌;热处理;预处理;

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