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Modelling of devolatilization in circulating fluidized bed combustion

机译:循环流化床燃烧脱挥发型建模

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A mathematical model is developed to describe the devolatilization process in a circulating fluidized bed combustor. The model is a combination of two submodels: single particle devolatilization and fluid dynamics. The single particle modelincludes the influence of both chemical kinetics and heat transfer on the rate of devolatilization. The results show a good agreement with literature data. The fluid dynamic model describes the main characteristics of a CFB: A dense zone in the bottom,followed by a splash zone and a dilute zone with a core-annulus structure. Each zone is modelled as a number of CSTR's and the size and number of CSTR's has been estimated from tracer experiments in an 80 MW{sub}(th) CFB boiler. It was not possible toevaluate the model against experimental data, but the dependence of particle size on the degree of devolatilization in the dense bed agrees qualitative with the expected behavior. The model shows that the devolatilization mainly occurs in the dense bed.
机译:开发了一种数学模型来描述循环流化床燃烧器中的脱挥石过程。该模型是两个子模型的组合:单粒子脱挥石和流体动力学。单粒子模型包括化学动力学和传热对脱挥发率的影响。结果表明,与文献数据吻合良好。流体动力学模型描述了CFB的主要特性:底部的致密区,其次是溅射区和具有芯环结构的稀释区。每个区域都被建模为许多CSTR的数据,并且CSTR的大小和数量已经从80 MW {Sub}(Th)CFB锅炉中的示踪实验估计。无法向实验数据进行模型,但粒径对致密床中脱挥发程度的依赖性同意与预期行为的定性。该模型表明,脱挥发化主要发生在密集的床中。

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