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Numerical investigation into the effect of burner swirl direction on furnace and superheater heat absorption for a 620 MWe opposing wall-fired pulverized coal boiler

机译:燃烧器旋流方向对620 MWE相对壁烧煤煤锅炉炉旋流方向对炉膛和过热器吸热作用的数值研究

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The paper investigates the effects of pulverized coal swirl burners' secondary air swirl directions on furnace water-wall, platen superheater and high temperature superheater heat absorption by using numerical simulations. The resultant effect on the carbon-monoxide and unburnt carbon levels was also investigated to establish the furnace performance. The conventional RANS approach was used along with a two-equation turbulence closure model to simulate the multispecies gas phase flow. Fuel particles were modeled as a discrete phase. The gas phase combustion was simulated using the eddy dissipation finite rate kinetics model and the surface reactions using a diffusion-kinetics limited model. To establish the validity of the modelling approach an actual 620 MWe boiler furnace and its superheaters were modelled, and the results compared to processed plant data. Once the model showed that it can predict the plant performance with reasonable accuracy it was used to investigate the performance changes for various burner swirl arrangements. Six swirl arrangement cases were simulated to determine the effect on the furnace performance indicators. It was found that by swirling all the burners per wall in the same direction that the furnace heat absorption could be increased by up to 6.67% and the unburned carbon fraction reduced from 0.029% to 0.022% when compared to the current boiler swirl configuration results, which has a staggered swirl direction arrangement. Furthermore, it was shown that the enhanced mixing in the volume adjacent to the burners also reduced the carbon-monoxide levels. The simulations demonstrated, for the given modelling methodology, that there is indeed interaction between adjacent burners which influences the combustion rate and in turn heat absorption in the water-cooled furnace walls and platen superheater for the modelled boiler. (C) 2019 Elsevier Ltd. All rights reserved.
机译:本文通过使用数值模拟调查了粉煤旋转燃烧器二次空气旋流方向对炉水墙,压板过热器和高温过热器吸热的影响。还研究了对一氧化碳和未燃烧碳水平的产生效果,以建立炉子性能。传统的RAN方法以及双等式湍流闭合模型一起使用,以模拟多数气相流。燃料颗粒被建模为离散阶段。使用涡流耗散有限速率动力学模型和使用扩散动力学有限公司模型模拟气相燃烧。为了建立建模方法的有效性,建模实际的620 MWE锅炉炉及​​其过热剂,与加工植物数据相比,结果。一旦模型显示它可以以合理的准确性预测植物性能,它用于研究各种燃烧器旋流装置的性能变化。模拟六个旋流排列案例以确定对炉子性能指标的影响。结果发现,与电流锅炉旋流配置结果相比,每墙上的每个壁的每个壁的所有燃烧器相同的方向旋转炉吸热,并且未燃烧的碳馏分从0.029%降低0.022%,有一个交错的旋流方向安排。此外,显示与燃烧器相邻的体积中的增强混合也降低了碳一氧化碳水平。对于给定的建模方法,模拟表明,相邻燃烧器之间存在确实相互作用,其影响燃烧速率和在水冷炉壁和用于模型锅炉的压板过热器中的热吸收。 (c)2019 Elsevier Ltd.保留所有权利。

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