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A novel integrated single-stage anaerobic co-digestion and oxidation ditch-membrane bioreactor system for food waste management and building wastewater recycling

机译:一种新型综合单阶段厌氧共消化和氧化沟膜生物反应器系统,用于食品废物管理和建筑废水再循环

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This study is to develop a novel integrated single-stage anaerobic co-digestion and oxidation ditch membrane bioreactor (SAC/OD-MBR) for food waste and building wastewater recycling. The co-digestion of food waste (FW) from a canteen with waste sludge (WS) from OD-MBR was performed with the proportion of FW:WS at 10:1 by weight. The liquid digestate from the co-digestion process was further co-treated with building wastewater in the OD-MBR system for water reuse purpose. Maximum methane content of 65.2% in biogas as well as average specific methane yield of 0.24 gCH_4/gVS could be obtained with anaerobic co-digestion of food waste and waste sludge from OD-MBR with HRT of 24 h and horizontal flow velocity of 0.3 m/s. The observed main methanogen species in this co-digestion process were Methanoculleus bourgensis and Methanoculleus palmolei. For co-treatment of liquid digestate and building wastewater with the OD-MBR, it was found that HRT of 24 h and horizontal flow velocity of 0.3 m/s could achieve highest COD and nitrogen removal efficiencies. HRT can be considered as a main key parameter to promote nitrification activity inside the OD-MBR system. Moreover, treated effluent from the SAC/OD-MBR could comply with the water reuse standard for garden and landscape application in the university campus. Furthermore, the techno-economic analysis indicates that this proposed system has a high potential of total cost savings and other indirect benefits. Therefore, the prototype SAC/OD-MBR can be an alternative system for food waste management and wastewater recycling for building application.
机译:本研究是开发一种新型的整合单级厌氧共消化和氧化沟膜生物反应器(SAC / OD-MBR),用于食物垃圾和建筑废水再循环。用来自OD-MBR的食物废物(FW)与来自OD-MBR的废污泥(WS)的食物废物(FW)的共消化杂交(FW)的比例进行:WS在10:1重量的比例进行。通过在OD-MBR系统中进一步共同处理来自共消化过程的液体消化方法,用于水重用目的。在OD-MBR与24小时的HRT的OD-MBR和0.3米的HRT的厌氧共消化食物废物和废污泥的厌氧共消化,最大甲烷含量为65.2%的沼气和平均甲烷产率为0.24gCH_4 / GV。 / s。在该共消化过程中观察到的主要甲基甲烷物种是甲烷素植物和Methanoculleus palmolei。对于液体消化和与OD-MBR建造废水的合作,发现24小时的HRT和0.3m / s的水平流速可以实现最高的COD和氮去除效率。 HRT可以被认为是促进OD-MBR系统内的硝化活动的主要关键参数。此外,来自SAC / OD-MBR的处理流出物可以符合大学校园的花园和景观应用的水重用标准。此外,技术经济分析表明,这一提出的系统具有高潜力的总成本节约和其他间接效益。因此,原型SAC / OD-MBR可以是用于建筑应用的食品废物管理和废水回收的替代系统。

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