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Modeling of the axial distributions of volatile species in a circulating fluidized bed boiler

机译:循环流化床锅炉挥发物种轴向分布的建模

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The proper understanding and description of the spatial distributions of volatile species is important to the circulating fluidized bed (CFB) reactor design and modeling. Aiming at this issue, a mathematical model has been developed in the present work, which constitutes of two main modules that are validated by experiments, one-dimensional fluid dynamic model and single fuel particle devolatilization model. The simulation of a 135 MWe CFB boiler was conducted. Results show that all volatile species exhibit in general a vertical release profile of bimodal shape (coal inlet area and bottom dense bed) while with quantitative differences, which is mainly attributed to the wide size range of feeding fuel. Compared to the influence of bed temperature, the effect of feeding coal size on the volatile nitrogen release is more obvious. This model can be applied as the devolatilization sub-model for the integral combustion simulation of a CFB boiler. (C) 2021 Elsevier Ltd. All rights reserved.
机译:正确理解和描述挥发性物质的空间分布对循环流化床(CFB)反应器的设计和建模非常重要。针对这一问题,本文建立了一个数学模型,该模型由两个主要模块组成,并通过实验进行了验证:一维流体动力学模型和单燃料颗粒脱挥模型。对135mwe循环流化床锅炉进行了模拟计算。结果表明,所有挥发性组分总体上呈现双峰形状(煤入口区和底部密层)的垂直释放剖面,但存在数量差异,这主要归因于进料燃料的大尺寸范围。与床层温度相比,给煤粒度对挥发氮释放的影响更为明显。该模型可作为CFB锅炉整体燃烧模拟的脱挥子模型。(c)2021爱思唯尔有限公司保留所有权利。

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