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Co-digestion Approaches to Organic Fraction of Municipal Solid Waste with Primary Sludge for a Municipal Treatment Plant in Turkey

机译:土耳其市政治疗厂初级污泥的城市固体废物有机分数的共消化方法

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The comparison of wet anaerobic digesters fed with differently sorted organic fraction of municipal solid waste (OFMSW) was carried out by co-digestion approaches to the primary sludge taken from Kayseri municipal wastewater treatment plant (WWTP) located in the Central Anatolian Region of Turkey. The WWTP was designed in two stages. The second mesophilic anaerobic digester is planned to be constructed after 20 years in the second stage. In this study, the construction of the second digester and a pre-treatment unit for municipal solid waste were proposed in the current stage for co-digestion purposes. Two alternatives were proposed using different solid waste contents in the co-digesters. In order to provide the required solid content, some amount of the treated wastewater was recycled to each digester together with the primary sludge. Although the existing collection method was assumed to be characterized as mechanical sorted (MS-OFMSW) (Option 1), source sorted (SS-OFMSW) alternative was also evaluated in the study (Option 2). The total energy demand of Kayseri WWTP was reported as around 42,300 kWh per day. Utilizing the energy produced by the digester, only 30% of the total energy demand and all of the heat energy demand including administration building can be covered. Thus, the aim was to evaluate how energy production would be increased by the application of co-digestion of OFMSW together with the primary sludge in Kayseri WWTP. Results indicated that the best operational condition in the cases of organic loading rate (OLR), hydraulic retention time (HRT) and energy recovery could be provided using 10% solid content in each co-digester for both options. According to the approach in Option 1, almost 77% of the total energy demand could be covered by applying co-digestion of MS-OFMSW together with the primary sludge and 200 m3 treated wastewater recycle. On the other hand, almost 100% energy recovery could be obtained when co-digestion approach (Option 2) was performed according to SS-OFMSW together with the primary sludge at 150 m~3 treated wastewater recycle. Significant amounts of sludge cakes (anaerobic compost) were produced after co-digestion and aerobic composting could be considered as an appropriate post treatment alternative. Co-digestion of OFMSW and sewage sludge may be an attractive alternative for sustainable management of two separate waste streams produced at large amounts in the developing countries.
机译:通过来自位于土耳其中央阿纳托利亚地区的Kayseri市政废水处理厂(WWTP)的初级污泥进行了不同分选有机物(OFMSW)的湿厌氧消化器的比较。 WWTP有两个阶段设计。第二次嗜合厌氧蒸煮器计划在第二阶段20年后构建。在本研究中,在当前阶段提出了第二档的构建和城市固体废物的预处理单元以进行共消化目的。在共消化器中使用不同的固体废物含量提出了两种替代方案。为了提供所需的固体含量,将一定量的处理废水与初级污泥一起再循环至每种消化器。尽管假设现有的收集方法表征为机械分类(MS-OFSW)(选项1),但在研究中也评估了源分类(SS-OFMSW)替代方案(选项2)。 Kayseri WWTP的总能源需求报告为每天约42,300千瓦时。利用蒸煮器产生的能量,只能覆盖总能源需求的30%的总能源需求和所有热能需求。因此,目的是评估如何通过在Kayseri WWTP中的初级污泥中使用欧姆语的共消化来增加能量产生。结果表明,在有机加载速率(OLR),液压保留时间(HRT)和能量回收的情况下,可以在每个共蒸煮器中使用10%的固体含量来提供最佳的运行条件。根据选项1的方法,通过将MS-OFMS的共消化和初级污泥和200m3处理的废水再循环应用,可以通过将MS-OFMSW和200M3处理的废水再循环覆盖近77%的总能量需求。另一方面,当使用150m〜3处理的废水中的初级污泥将共消化方法(选件2)与初级污泥一起进行时,可以获得几乎100%的能量回收。在共消化和有氧堆肥之后生产大量的污泥蛋糕(厌氧堆肥)可以被认为是适当的后处理替代品。对MSW和污水污泥的共同消化可能是在发展中国家大量生产的两个单独废物流的可持续管理的有吸引力的替代方案。

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