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首页> 外文期刊>Waste Management >Single-phase anaerobic digestion of the organic fraction of municipal solid waste without dilution: Reactor stability and process performance of small, decentralised plants
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Single-phase anaerobic digestion of the organic fraction of municipal solid waste without dilution: Reactor stability and process performance of small, decentralised plants

机译:单相厌氧消解城市固体废物的有机分数,无稀释:反应堆稳定性和工艺性能小,分散植物

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摘要

Currently, centralised plants are the most favoured approach for the anaerobic treatment of the organic fraction of municipal solid waste (OFMSW). However, centralised solutions imply certain environmental impacts, which prevent large-scale implementation of the anaerobic digestion (AD). As a result, we are digesting <5% of organic waste both in Europe and the USA even today. Pursuing the criteria for maximising the balance between profit and impacts, an innovative layout with the ultimate goal of promoting the use of small, decentralised AD plants is proposed. In this study, source-separated OFMSW (SS-OFMSW) was treated in a mesophilic plug flow reactor by applying an atypical combination of conditions such as high SS-OFMSW solid content (214.5 g·kg~(-1)), high organic loading rate (6.2 kg VS·m~(-3)-^1), and no dilution or co-substrate addition. A suitable and an efficient mixing system is essential to control the process. Accordingly, the process was stable in a single-stage reactor, in the absence of digestate recircula-tion, obtaining specific gas production of 0.67 m~3· kg~(-1)VS in terms of biogas and 0.41 m3·kg~(-1) VS in terms of methane. High reactor volume exploitation and small plant construction were feasible, reaching a gas production rate of 4.5 m~3·m~(-3) d~(-1). The estimated costs in terms of capital and operating expenditure are expected to realize gross economic sustainability of full-scale installation.
机译:目前,集中式植物是最有利的厌氧治疗城市固体废物(OFMSW)的厌氧处理方法。然而,集中式解决方案意味着某些环境影响,防止厌氧消化(AD)的大规模实施。因此,我们即使在今天在欧洲和美国消化5%的有机废物。提出了一种促进利润和影响之间平衡的标准,提出了一种创新的布局,促进了促进使用小型分散的广告植物的最终目标。在该研究中,通过施加诸如高SS-OFMSW固体含量(214.5g·kg〜(-1)),高有机的条件(214.5g·kg〜加载速率(6.2 kg vs·m〜(3) - ^ 1),无稀释或共衬底添加。合适的和有效的混合系统对于控制该过程至关重要。因此,该方法在单阶段反应器中稳定,在没有消化循环循环的情况下,在沼气和0.41m 3·kg〜(1)中获得0.67m〜3·kg〜(-1)Vs的特定气体产量。 -1)甲烷方面的vs。高反应器体积剥削和小植物结构是可行的,达到4.5米〜3·m〜(3)D〜(-1)的气体生产率。预计资本和经营支出方面的估计成本将实现全面安装的经济总体可持续性。

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  • 来源
    《Waste Management》 |2021年第4期|103-111|共9页
  • 作者单位

    Schmack Biogas srl Bolzano 39100 Italy Department of Environmental Sciences Informatics and Statistics Ca' Foscari University of Venice via Torino 155 Venice 30172 Italy;

    Department of Biotechnology University of Verona Strada Le Crazie Verona 37134 Italy;

    Department of Biotechnology University of Verona Strada Le Crazie Verona 37134 Italy;

    Department of Environmental Sciences Informatics and Statistics Ca' Foscari University of Venice via Torino 155 Venice 30172 Italy;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    SS-OFMSW; Food Waste; Mono-digestion; Anaerobic Digestion; Small Plant; Biogas;

    机译:SS-OFMSW;食物垃圾;单消化;厌氧消化;小植物;沼气;

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