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Relations between carbon removal rates, biofilm size and density of a novel anaerobic reactor: the inverse turbulent bed

机译:新型厌氧反应器除碳速率,生物膜尺寸和密度之间的关系:逆流床

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An anaerobic inverse turbulent bed, in which the biogas only ensures fluidisation of floating carrier particles, was investigated for carbon removal kinetics and for biofilm growth and detachment. The range of operation of the reactor was kept within 5 and 30 kg(COD).m(3).d(-1), with Hydraulic Retention Times between 0.28 and 1 day. The carbon removal efficiency remained between 70 and 85%. Biofilm size were rather low (between 5 and 30 mu m) while biofilm density reached very high values (over 80 kg(VS).m(-3)). The biofilm size and density varied with increasing carbon removal rates with opposite trends; as biofilm size increases, its density decreases. On the one hand, biomass activity within the reactor was kept at a high level, (between 0.23 and 0.75 kg(TOC).kg(VS).d(-1), i.e, between 0.6 and 1.85 kg(COD).kg(VS).d(-1)). This result indicates that high turbulence and shear may favour growth of thin, dense and active biofilms. It is thus an interesting tool for biomass control. On the other hand, volatile solid detachment increases quasi linearly with carbon removal rate and the total amount of solid in the reactor levels off at high OLR. This means that detachment could be a limit of the process at higher organic loading rates. [References: 11]
机译:研究了厌氧反向湍流床,其中的沼气只能确保漂浮的载体颗粒的流化,研究了除碳动力学以及生物膜的生长和分离。反应器的操作范围保持在5到30 kg(COD).m(3).d(-1),水力停留时间在0.28到1天之间。除碳效率保持在70%至85%之间。生物膜的大小相当低(5至30微米),而生物膜的密度却达到了很高的值(超过80 kg(VS).m(-3))。生物膜的大小和密度随着碳去除率的增加而变化,趋势相反。随着生物膜尺寸的增加,其密度降低。一方面,反应器内的生物质活性保持在较高水平(0.23至0.75 kg(TOC).kg(VS).d(-1)之间,即0.6至1.85 kg(COD).kg之间) (VS).d(-1))。该结果表明,高湍流和剪切力可能有利于薄,致密和活性生物膜的生长。因此,它是用于生物质控制的有趣工具。另一方面,挥发性有机物的去除随碳的去除率近似线性增加,并且在高OLR下反应器中的固体总量趋于稳定。这意味着在较高的有机负载率下,分离可能是该过程的限制。 [参考:11]

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