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机构地区:[1]上海电力学院,上海200090 [2]同济大学,上海200092
出 处:《煤气与热力》2005年第4期13-16,共4页Gas & Heat
摘 要:焦炭燃烧选取扩散-动力模型,煤热解反应采用双挥发竞争模型,气相湍流选取RNGk-ε模型,燃烧湍流选用PDF模型,采用CFD软件对1台装有32只双调风旋流燃烧器两侧墙对冲布置的1 025t/h燃煤锅炉炉内氮氧化物生成进行数值计算,研究了炉内温度场、氧浓度场以及氮氧化物浓度场的分布特性。发现三者在炉膛内均呈对称分布,燃烧区域内的温度和氮氧化物浓度较高而氧浓度较低,燃烧区域上方温度和氮氧化物浓度逐渐降低而氧浓度升高。研究了温度和空气系数对氮氧化物生成的影响,随着温度的升高,氮氧化物生成量呈升高趋势,而随着空气系数的增大,氮氧化物生成量呈降低趋势。By selecting diffusion kinetics model for coke combustion, two-competing-rates model for pyrolytic reaction of coal, RNG k-ε model for gas-phase turbulent flow, PDF model for combustion turbulent flow, the CFD software is used to numerically calculate NO_x formation in a coal-fired boiler of 1025 t/h. On the both side walls of the boiler, 32 swirl burners with double regulating air are arranged oppositely. The distribution characteristics of temperature field, NO_x and oxygen concentration field in furnace are studied, they are symmetrically distributed in furnace. In the combustion area, temperature and NO_x concentration are higher, while oxygen concentration is lower. Over the combustion (area), temperature and NO_x concentration are declined gradually, while oxygen concentration is raised. The effects of temperature and excess air coefficient on NO_x formation are discussed. The higher the temperature is, the more NO_x is formed. While the greater the excess air coefficient is, the less NO_x is formed.
分 类 号:TU995[建筑科学—供热、供燃气、通风及空调工程] TK229.6[建筑科学—市政工程]
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