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Reaction Kinetic Equation for Char Combustion of Underground Coal Gasification 被引量:2

Reaction Kinetic Equation for Char Combustion of Underground Coal Gasification
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摘要 Based on the quasi-steady-state approximation, the dynamic equation of char combustion in the oxidation zone of underground coal gasification (UCG) was derived. The parameters of the dynamic equation were determined at 900℃ using a thermo-gravimetric (TG) analyzer connected to a flue gas analyzer and this equation. The equation was simplified for specific coals, including high ash content, low ash content, and low ash fusibility ones. The results show that 1) the apparent reaction rate constant increases with an increase in volatile matter value as dry ash-free basis,2) the effective coefficient of diffusion decreases with an increase in ash as dry basis, and 3) the mass transfer coefficient is independent of coal quality on the whole. The apparent reaction rate constant, mass-transfer coefficient and effective coefficient of diffusion of six char samples range from 7.51×104 m/s to 8.98×104 m/s, 3.05×106 m/s to 3.23×106 m/s and 5.36×106 m2/s to 8.23×106 m2/s at 900℃, respectively. Based on the quasi-steady-state approximation, the dynamic equation of char combustion in the oxidation zone of underground coal gasification (UCG) was derived. The parameters of the dynamic equation were determined at 900℃ using a thermo-gravimetric (TG) analyzer connected to a flue gas analyzer and this equation. The equation was simplified for'specific coals, including high ash content, low ash content, and low ash fusibility ones, The results show that 1) the apparent reaction rate constant increases with an increase in volatile matter value as dry ash-free basis, 2) the effective coefficient of diffusion decreases with an increase in ash as dry basis, and 3) the mass transfer coefficient is independent of coal quality on the whole. The apparent reaction rate constant, mass-transfer coefficient and effective coefficient of diffusion of six char samples range from 7.51×10^4 m/s to 8.98×10^4 m/s, 3.05×10^6 m/s to 3.23×10^6 m/s and 5.36×10^6 m^2/s to 8.23×10^6m^2/s at 900℃, respectively.
出处 《Journal of China University of Mining and Technology》 EI 2006年第2期141-146,共6页 中国矿业大学学报(英文版)
基金 Projects 59906014, 50276066 and 20207014 supported by National Natural Science Foundation of China
关键词 underground coal gasification CHAR COMBUSTION kinetic equation thermo-gravimetric 地下煤气化 焦化 燃烧 动力方程
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  • 1黄镇宇,浙江大学学报,1986年,20卷,6期,46页
  • 2岑可法,1978年

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