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Mechanistic model for electricity generation via biomethane production through anaerobic digestion of organic fraction of municipal solid waste generated in Sri Lanka

机译:斯里兰卡产生的城市固体废物有机部分厌氧消化通过生物甲烷生产来发电的机械模型

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Waste management practices such as open dumping and composting are widely used for the management of municipal solid waste (MSW) in Sri Lanka. Severe socio-economic and environmental problems occur due to open dumping of major fraction of MSW. Anaerobic digestion is a sustainable waste management strategy to manage organic fraction of MSW (OFMSW). In order to evaluate the feasibility of this strategy, a mechanistic model was developed using a steady state anaerobic digestion model which was modified using improved Chen-Hashimoto kinetic equations. It was applied to treat OFMSW generated in open dumping site at Karadiyana in Sri Lanka. The daily MSW arrival to the site is 550 tons/day and input OFMSW slurry to the anaerobic bioreactor contained of total solids 70 g/l, volatile solids 55.6 g/l, carbohydrates 58.5%, proteins 13% and lipids 3%. According to the mechanistic model, minimum payback period of 1.79 years was achieved when anaerobic bioreactor operated in continuously fed mode at operating temperature of 40°C and hydraulic retention time of 11.28 days. The volatile solid reduction efficiency of 76.62%, methane yield of 0.26 m per kg of volatile solids added, electricity generation of 10.31 W per kg of OFMSW per day and carbon dioxide generation of 0.21 kg per kg of OFMSW were achieved at these optimized process conditions. The model was limited to apply for continuously fed anaerobic bioreactors operated at temperature ranging from 30°C to 40°C.
机译:诸如露天倾倒和堆肥之类的废物管理实践被广泛用于斯里兰卡的城市固体废物(MSW)的管理。由于大部分城市固体废弃物的公开倾倒,造成了严重的社会经济和环境问题。厌氧消化是一种可持续的废物管理策略,用于管理MSW(OFMSW)的有机部分。为了评估该策略的可行性,使用稳态厌氧消化模型开发了一种机械模型,该模型使用改进的Chen-Hashimoto动力学方程进行了修改。它被用于处理斯里兰卡Karadiyana露天倾倒场中产生的OFMSW。每天到达现场的城市固体废弃物为550吨/天,将OFMSW浆液输入到厌氧生物反应器中,其中总固体含量为70 g / l,挥发性固体含量为55.6 g / l,碳水化合物为58.5 \%,蛋白质为13 \%,脂质为3 \% 。根据该机理模型,当厌氧生物反应器在40°C的工作温度和11.28天的水力停留时间下以连续进料模式运行时,可实现1.79年的最低投资回收期。通过这些优化的工艺,挥发性固体的还原效率为76.62%,每千克挥发性固体添加的甲烷产量为0.26 m,每千克OFMSW每天发电10.31 W,每千克OFMSW产生二氧化碳为0.21 kg情况。该模型仅限于在30°C至40°C的温度范围内运行的连续进料厌氧生物反应器中使用。

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