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首页> 外文期刊>Renewable energy >Performance of an anaerobic fluidized bed bioreactor (AnFBR) for digestion of primary municipal wastewater treatment biosolids and bioethanol thin stillage
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Performance of an anaerobic fluidized bed bioreactor (AnFBR) for digestion of primary municipal wastewater treatment biosolids and bioethanol thin stillage

机译:厌氧流化床生物反应器(AnFBR)消化主要市政废水处理生物固体和生物乙醇稀釜馏物的性能

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摘要

The primary objective of this work was to investigate and compare the treatability of very high suspended solids with different biodegradable particulate fractions and COD fractionation, thin stillage (a by-product from the corn ethanol industry) as well as primary sludge from municipal wastewater treatment, using an anaerobic fluidized bed bioreactor (AnFBR) employing US Mesh 30 × 40 zeolite with a diameter of (d_m) in the range of 425-610 μm and specific surface area (SSA) of 26.5 m~2/g as the carrier media. Each experimental run lasted over a six-month period. Due to the long-term impact of accumulation of inert suspended solids in the AnFBR and potential active biomass washout leading to failure, treatability of high suspended-solid streams can be very challenging. Despite the very high strength of thin stillage and primary sludge with chemical oxygen demand of 130,000 mg TCOD/L and 42,000 mg TCOD/L respectively and suspended solids of 47,000 mg TSS/L and 34,000 mg TSS/L, the AnFBR showed, up to 88% and 82% TCOD and 78% and 82% TSS removal efficiencies from thin stillage and primary sludge respectively at very high organic and solids loading rates (OLR and SLR) of 29 kg COD/m~3 d and 9.5 kg COD/m~3 d and 10.5 kg TSS/m~3 d and 10.3 kg TSS/m~3 d respectively at hydraulic retention time (HRT) of 3.5 and 4 days. Maximum methane production yields of up to 0.31 L_(CH_4)/g_(COD) and 0.25 L_(CH_4)/g_(COD) were achieved for thin stillage and primary sludge respectively corresponding to biogas production rate per reactor volume of 15.8 L_(gas)/L_(reactor) d and 1.22 L_(CH_4)/L_(reactor) d.
机译:这项工作的主要目的是研究和比较具有不同生物可降解颗粒部分和COD分馏,稀釜馏物(玉米乙醇工业的副产品)以及市政废水处理产生的初级污泥的极高悬浮固体的可处理性,使用厌氧流化床生物反应器(AnFBR),将直径(d_m)在425-610μm,比表面积(SSA)为26.5 m〜2 / g的US Mesh 30×40沸石作为载体介质。每个实验运行持续六个月。由于惰性悬浮固体在AnFBR中积累的长期影响以及潜在的活性生物质冲刷导致失效,因此高悬浮固体流的可处理性可能非常具有挑战性。尽管稀薄釜馏物和初级污泥具有很高的强度,化学需氧量分别为130,000 mg TCOD / L和42,000 mg TCOD / L,悬浮固体含量分别为47,000 mg TSS / L和34,000 mg TSS / L,但直到在29 kg COD / m〜3 d和9.5 kg COD / m的非常高的有机物和固体装载量(OLR和SLR)下,稀薄釜馏物和初级污泥的TCOD去除效率分别为88%和78%和82%,TSS去除效率在水力停留时间(HRT)为3.5天和4天时,分别约为〜3 d和10.5 kg TSS / m〜3 d和10.3 kg TSS / m〜3 d。稀釜馏物和一次污泥的最大甲烷产量分别达到0.31 L_(CH_4)/ g_(COD)和0.25 L_(CH_4)/ g_(COD),分别对应于每反应器体积的沼气生产率15.8 L_(gas) )/ L_(反应器)d和1.22 L_(CH_4)/ L_(反应器)d。

著录项

  • 来源
    《Renewable energy》 |2014年第11期|276-285|共10页
  • 作者单位

    Department of Technical and R&D, Environmental Operating Solutions (EOSi), 160 MacArthur Blvd., Suite #6, Bourne, MA, 02532, USA;

    Department of Civil and Environmental Engineering, University of Waterloo, 200 University Avenue West, Waterloo, Ontario, N2L 3G1, Canada;

    Department of Civil and Environmental Engineering, University of Western Ontario, 1151 Richmodn Street, London, Ontario, N6A 5B9, Canada;

    GreenField Ethanol Inc., Chatham, Ontario, N7M 5J4, Canada;

    Department of Chemical and Biochemical Engineering, University of Western Ontario, London, Ontario, N6A 5B9, Canada;

    Department of Chemical and Biochemical Engineering, University of Western Ontario, London, Ontario, N6A 5B9, Canada;

  • 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

    Biosolids; Primary sludge; Thin stillage; High rate anaerobic digester; Fluidized bed bioreactor;

    机译:生物固体初级污泥;稀釜山;高速率厌氧消化器;流化床生物反应器;

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