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Modelling of slag deposition and flow characteristics of coal combustion under oxy-firing condition in a 550 MW tangentially fired furnace

机译:550 MW切向燃烧炉中氧燃烧条件下煤渣沉积和流动特性的模拟

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In this paper, the development of three dimensional slagging combustion model for coal-firing in a 500 MW tangentially fired industrial furnace under oxy-fuel condition is presented. The model incorporates the Eulerian-Lagrangian model for the gas-particles flow and the particles-wall interaction sub model for predicting the deposition and conversion characteristics of char/ash particles. A commercial CFD package coupled with some user-defined functions were used for consideration of char particle combustion and tracking, particle capturing and deposition and other related phenomenons. Validation of the model was achieved by comparing the available slag thickness data for coal-water slurry combustion under oxy-fuel condition in a 5 MW small scale furnace. The slag thickness deposited on the furnace wall was found to be in good agreement with the available data. Species distributions such as O-2, CO2, H2O, flame temperature distribution and flow dynamics were presented at different heights. Coal particles appeared to be combusted at a relatively higher rate in the near burner region and burn in situ because of enriched O-2 concentration. The deposited slag thicknesses on the vertical wall of reaction zone were found in the range of 0-1.0 mm. Due to the effect of gravitational force, the molten slag flows downward and velocity was slow (maximum 0.05 mm/s) because of higher viscosity and greater surface tension properties. Overall, this study provides an understanding of how the ash/char particles are deposited on the refractory wall and its dynamics in an industrial furnace. (C) 2016 Published by Elsevier Ltd.
机译:本文提出了一种在氧气-燃料条件下500 MW切向燃烧工业炉中燃煤的三维排渣燃烧模型的开发方法。该模型结合了用于气体颗粒流动的欧拉-拉格朗日模型和用于预测炭/灰颗粒沉积和转化特性的颗粒-壁相互作用子模型。商业CFD程序包结合一些用户定义的功能用于考虑炭颗粒燃烧和跟踪,颗粒捕获和沉积以及其他相关现象。通过比较5兆瓦小型炉中氧燃料条件下水煤浆燃烧的可用炉渣厚度数据,对模型进行了验证。发现沉积在炉壁上的炉渣厚度与现有数据高度吻合。 O-2,CO2,H2O,火焰温度分布和流动动力学等物种分布在不同的高度出现。由于富含O-2的浓度,煤颗粒似乎在燃烧器附近以较高的速率燃烧,并就地燃烧。发现在反应区的垂直壁上沉积的炉渣厚度在0-1.0mm的范围内。由于重力的作用,由于较高的粘度和较大的表面张力性能,熔融炉渣向下流动,速度很慢(最大0.05 mm / s)。总的来说,这项研究使人们了解了灰/炭颗粒如何沉积在耐火材料壁上以及在工业炉中的动力学。 (C)2016由Elsevier Ltd.出版

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