Connelly Stephanie, Shin Seung G, Dillon Robert J, Ijaz Umer Z, Quince Christopher, Sloan William T, Collins Gavin
Infrastructure and Environment, School of Engineering, University of GlasgowGlasgow, UK.
School of Environmental Science and Engineering, Pohang University of Science and TechnologyPohang, South Korea.
Front Microbiol. 2017 May 1;8:664. doi: 10.3389/fmicb.2017.00664. eCollection 2017.
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, 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 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.
研究新型或改良生物技术(如污水处理消化器)的可行性时,不可避免地要从实验室规模的试验开始。然而,很少有人确定实验室规模的结果是否能反映全尺寸性能或微生物生态学。本研究以膨胀颗粒污泥床(EGSB)生物反应器为模型,该反应器是一种高速厌氧消化器配置,旨在填补这一知识空白。构建了EGSB的两种实验室规模理想化模型——全尺寸设计的一维和三维缩小模型,并在与全尺寸EGSB几乎相同的条件下一式三份运行。实验室规模的生物反应器使用从全尺寸生物反应器获得的生物质进行接种,并将玉米威士忌蒸馏产生的废水作为两种规模的底物。在70多天的时间里,使用16S rRNA基因测序(V4区域)、特定产甲烷活性(SMA)测定以及一系列物理和化学监测方法,在污泥床的不同深度监测生物反应器性能、微生物生态学和微生物群落生理学。SMA测定表明,全尺寸时氢营养途径占主导地位,而在实验室规模试验期间形成了更平衡的活性分布。在每个规模下, 都是主要的产甲烷菌属。总体而言,实验室规模的生物反应器性能优于全尺寸。我们观察到,实验室规模的生物反应器设计显著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,一维生物反应器类型促进了两者的分层。在一维实验室生物反应器中, 的丰度增加与污泥床中颗粒的位置以及以乙酸盐和乙醇为底物时活性的增加有关。我们进一步观察到,一维实验室规模生物反应器中污泥床的分层与物种(OTU)水平下潜在微生物群落丰富度的增加以及整体性能的改善有关。