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NUMERICAL MODEL FOR THE DYNAMIC SIMULATION OF A LARGE SCALE COMPOSTING SYSTEM

机译:大型组合系统动态仿真的数值模型。

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摘要

A numerical model simulating airflow pattern, heat and mass transfer, and degradation in the two dimensional cross-section of a deep bed composting vessel was developed. The model accounts for compressibility of the material and predicts spatial and temporal changes in state variables. The model was validated at a commercial facility that composts a mix of biosolids, bark and sawdust. Simulations were performed to quantify the effects of (1) initial moisture level, (2) depth of bed, (3) ambient air temperature, (4) cooling air recirculation, (5) material degradability and (6) blockage of plenum, on cost of aeration and spatial homogeneity of degradation within the vessel. Results show that cost of aeration is lowest when the material is at an initial moisture level of 55% and the bed depth is 3.5 m. Energy required per unit of dry matter degraded decreases as the ambient temperature increases. The increased aeration requirement when cooling air was recirculated was quantified, and shows that overall energy requirements are reduced by recirculating air. Aeration energy requirements and system throughput were compared under different operating parameters.
机译:建立了数值模型,模拟了深床堆肥容器的二维横截面中的气流模式,传热和传质以及降解。该模型考虑了材料的可压缩性,并预测状态变量的时空变化。该模型已在将生物固体,树皮和锯末混合而成的商业设施中进行了验证。进行模拟以量化以下各项对以下方面的影响:(1)初始湿度,(2)床深,(3)环境温度,(4)冷却空气再循环,(5)材料降解性和(6)通风系统堵塞。曝气成本和容器内降解的空间均匀性。结果表明,当材料的初始湿度为55%且床层深度为3.5 m时,曝气成本最低。每单位降解的干物质所需的能量随环境温度的升高而降低。量化了冷却空气再循环时增加的曝气需求,表明通过再循环空气降低了总能量需求。比较了不同运行参数下的曝气能量需求和系统通量。

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