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Bioreactor Scalability: Laboratory-Scale Bioreactor Design Influences Performance Ecology and Community Physiology in Expanded Granular Sludge Bed Bioreactors

机译:生物反应器的可扩展性:实验室规模的生物反应器设计影响膨胀的颗粒污泥床生物反应器的性能生态和群落生理

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摘要

Studies investigating the feasibility of new, or improved, biotechnologies, such as wastewater treatment digesters, inevitably start with laboratory-scale trials. However, it is rarely determined whether laboratory-scale results reflect full-scale performance or microbial ecology. The Expanded Granular Sludge Bed (EGSB) bioreactor, which is a high-rate anaerobic digester configuration, was used as a model to address that knowledge gap in this study. Two laboratory-scale idealizations of the EGSB—a one-dimensional and a three- dimensional scale-down of a full-scale design—were built and operated in triplicate under near-identical conditions to a full-scale EGSB. The laboratory-scale bioreactors were seeded using biomass obtained from the full-scale bioreactor, and, spent water from the distillation of whisky from maize was applied as substrate at both scales. Over 70 days, bioreactor performance, microbial ecology, and microbial community physiology were monitored at various depths in the sludge-beds using 16S rRNA gene sequencing (V4 region), specific methanogenic activity (SMA) assays, and a range of physical and chemical monitoring methods. SMA assays indicated dominance of the hydrogenotrophic pathway at full-scale whilst a more balanced activity profile developed during the laboratory-scale trials. At each scale, Methanobacterium was the dominant methanogenic genus present. Bioreactor performance overall was better at laboratory-scale than full-scale. We observed that bioreactor design at laboratory-scale significantly influenced spatial distribution of microbial community physiology and taxonomy in the bioreactor sludge-bed, with 1-D bioreactor types promoting stratification of each. In the 1-D laboratory bioreactors, increased abundance of Firmicutes was associated with both granule position in the sludge bed and increased activity against acetate and ethanol as substrates. We further observed that stratification in the sludge-bed in 1-D laboratory-scale bioreactors was associated with increased richness in the underlying microbial community at species (OTU) level and improved overall performance.
机译:研究新的或改进的生物技术(例如废水处理沼气池)的可行性的研究不可避免地从实验室规模的试验开始。但是,很少确定实验室规模的结果是否能反映出全面的性能或微生物生态学。膨化颗粒污泥床(EGSB)生物反应器是一种高速厌氧消化器,在研究中被用作解决该知识缺口的模型。 EGSB的两个实验室规模的理想化(一维设计和一维三维缩小)是一个完整的设计,并且在接近完全相同的条件下一式三份地运行到一个完整的EGSB。使用从全尺寸生物反应器获得的生物量播种实验室规模的生物反应器,并以两种规模将来自玉米威士忌蒸馏的废水用作底物。在超过70天的时间里,使用16S rRNA基因测序(V4区域),特定的产甲烷活性(SMA)分析以及一系列的物理和化学监测,对污泥床中不同深度的生物反应器性能,微生物生态学和微生物群落生理学进行了监测。方法。 SMA分析表明,在整个规模的氢营养途径中占主导地位,而在实验室规模的试验过程中,活性分布更加平衡。在各个规模上,甲烷菌是目前占主导地位的产甲烷菌属。在实验室规模上,生物反应器的总体性能要好于全面规模。我们观察到,实验室规模的生物反应器设计显着影响了生物反应器污泥床中微生物群落生理学和分类学的空间分布,其中一维生物反应器类型可促进每种生物的分层。在1-D实验室生物反应器中,Firmicutes的丰度增加与污泥床中的颗粒位置以及对作为底物的乙酸盐和乙醇的活性增加有关。我们进一步观察到,在一维实验室规模的生物反应器中,污泥床中的分层与物种(OTU)水平上底层微生物群落的丰富度增加和整体性能提高相关。

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