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Dynamic behaviour of sewage sludge incineration in a large-scale bubbling fluidised bed in relation to feeding-rate variations

机译:大型鼓泡流化床中污泥焚烧的动态行为与进料速度的变化

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In this paper, a mathematical model is developed for the simulation of a large-scale sewage sludge incineration plant. The model assumes the bed to consist of a fast gas phase, an emulsion phase and a fuel particle phase with specific consideration for thermally-thick fuel particles. The developed model is employed to predict the dynamic response of the bed combustion to fluctuations in sludge feeding-rate. Calculation results indicate that the bed combustion is sensitive to fluctuations with response times greater than 30 min, but severe delays exist for both outlet oxygen level and bed temperatures; from 6 to 13 min for O_2 and 22-45 min for temperatures. Depending on the fluctuation frequency, the corresponding phase shifts are 39-96° for outlet O_2, 138-336° for bed temperature and 80-336° for freeboard temperature.
机译:本文为大型污水污泥焚烧厂的仿真开发了数学模型。该模型假定床层由快速气相,乳化相和燃料颗粒相组成,并特别考虑了热厚燃料颗粒。所开发的模型用于预测床层燃烧对污泥进料速率波动的动态响应。计算结果表明,床层燃烧对响应时间大于30分钟的波动敏感,但出口氧气水平和床层温度均存在严重的延迟。 O_2为6到13分钟,温度为22-45分钟。根据波动频率,出口O_2的相应相移为39-96°,床温为138-336°,干舷温度为80-336°。

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