首页|鼓泡床条件下石墨颗粒燃烧行为的试验与模型研究

鼓泡床条件下石墨颗粒燃烧行为的试验与模型研究

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通过鼓泡床焚烧方式可以实现对废弃石墨的大幅减容,为了探究石墨在鼓泡床内的燃烧行为,以单石墨颗粒为研究对象,利用鼓泡床试验台对其燃烧特性开展了试验研究,并结合数学模型分析了床层温度、床料粒径、石墨粒径等因素的影响关系.结果表明:鼓泡床层温度的降低和流化风速的增加都会使得烟气中 CO浓度增加;随着床层温度由 700℃增加至 900℃,石墨颗粒燃烧速率逐渐加快,但增加幅度逐渐减小,显示出燃烧由化学反应控制逐渐转向传质过程控制,在 900℃时的燃烧速率主要受传质过程影响;在满足了最小流化风速的前提下,提高鼓泡床内流化风速不能显著增加床层内的气相传质系数;石墨粒径的减小和床料粒径的增加均能提高床层内的传质系数,从而促进比燃烧速率的增加.
Experimental and Model Study on Combustion Behavior of Graphite Particles in Bubbling Bed
The substantial reduction of waste graphite can be achiered by bubbing bed com-busting.In order to explore the combustion behavior of graphite in bubbling bed,the com-bustion characteristics of graphite particles were investigated by bubbling bed test bench,and the influence of bed temperature,bed particle size,graphite particle size and other factors was analyzed by mathematical model.The results show that the CO concentration in flue gas in-creases with the decrease of bubbling bed temperature and the increase of fluidizing wind speed.As the bed temperature increases from 700℃ to 900℃,the combustion rate of graph-ite particles increases gradually,but the increase amplitude decreases gradually,showing that the control of chemical reaction gradually changes to the control of mass transfer process.At 900℃,the combustion rate of graphite is mainly affected by the mass transfer process.Under the premise of meeting the minimum fluidizing wind speed,increasing the fluidizing wind speed in bubbling bed cannot significantly increase the mass transfer coefficient in the bed.Both the decrease of graphite particle size and the increase of bed particle size can improve the mass transfer coefficient in the bed,thus promoting the increase of specific combustion rate.

combustion behavior of graphitemathematical modelbubbling bed combustion

赵强、周托、金燕、黄增辉

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太原理工大学 电气与动力工程学院,山西 太原 030024

清华大学 能源与动力工程系,北京 100084

中国矿业大学(北京)化学与环境工程学院,北京 100083

石墨燃烧行为 数学模型 鼓泡床燃烧

华能集团总部科技项目基础能源科技研究专项项目

HNKJ20-H50

2024

锅炉技术
上海锅炉厂有限公司

锅炉技术

北大核心
影响因子:0.409
ISSN:1672-4763
年,卷(期):2024.55(4)