摘要
以3种细度的混煤煤焦作为再燃燃料,用N2、O2、CO2和NO配制模拟烟气,在1200℃、1300℃和1400℃立管式携带炉中进行了再燃还原NO的实验研究,对其化学反应机理进行了分析。结果表明:微细化煤焦再燃还原NO的反应速率受扩散-反应动力学的联合控制。因此,提高再燃区温度水平、使用反应活性高的煤焦或提高再燃煤焦的细度,均能明显提高再燃还原NO的化学反应速率。
Experimental tests on NO reduction by reburning have been performed at 1200℃, 1300℃ and 1400℃, in an entraining tube furnace, using a mixture of coal char particles, with 3 different granularities, as the reburning fuel and a proper mixture of N2, 02, CO2, and NO as the simulated flue gas. The chemical reaction mechanism was therewith analyzed. Results indicate that the reducing reaction rate of NO depends upon the combined effect of diffusion and reaction kinetics. Therefore, the reducing reaction rate of NO can noticeably be increased by raising the temperature in the reburning zone and by using char of high reactivity or high granularity.
出处
《动力工程》
CSCD
北大核心
2007年第6期964-968,共5页
Power Engineering
基金
国家电力公司科技攻关资助项目(KJ000-02-16-03)
博士教师基金资助项目(20041203)
关键词
环境工程学
烟气脱硝
微细煤焦
再燃
NO
反应机理
environmental engineering
denitrification of flue gas
micronized coal coke
reburning
NO
reactionmechanism