合成气
燃烧
木材气体发生器
煤
锅炉(水暖)
废物管理
燃烧热
环境科学
合成气制汽油
核工程
工程类
化学
氢
蒸汽重整
制氢
有机化学
作者
Lichen Ren,Xinxin Shang,Jingjing Xie,Jiechao Chen,Yanan Gu
出处
期刊:ACS omega
[American Chemical Society]
日期:2024-12-05
卷期号:9 (50): 49387-49396
标识
DOI:10.1021/acsomega.4c06787
摘要
To comprehensively explore syngas cocombustion technology, gasification experiments in a bench-scale circulating fluidized bed (CFB) and three-dimensional (3D) numerical simulations of a coal-fired boiler furnace have been conducted. In the amplification experiment of biomass gasification, sawdust has been gasified using air, oxygen-enriched air, and steam. The highest heating value of the syngas products reaches 12.3 MJ/m3 when the equivalence and steam/biomass ratios are adjusted in the ranges of 0.21–0.31 and 0.1–0.5, respectively. Subsequently, 3D numerical simulation has been performed with several kinds of syngas product to analyze the cocombustion characteristics of the boiler furnace. Results demonstrate that the velocity field of the boiler furnace exhibits a well-formed tangential velocity circle and full degree of streamlines. Syngas cocombustion in the coal-fired furnace reduces the temperature extremum in the combustion zone. Radiant heat flux accounts for >88% of the total heat flux in the furnace. The outlet NO concentration in the case of syngas cocombustion is less than that of pure coal combustion, and it is reduced approximately 25 and 40 mg/m3 at cocombustion ratios of 0.1 and 0.15, respectively.
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