Experimental studies on two dimensional particle swarm gasification of different coal chars and petroleum coke at high temperature

被引:10
作者
Liu, Ming [1 ,2 ]
Shen, Zhongjie [1 ,2 ]
Liang, Qinfeng [1 ,2 ]
Xu, Jianliang [1 ,2 ]
Zhao, Hui [1 ,2 ]
Liu, Haifeng [1 ,2 ]
机构
[1] East China Univ Sci & Technol, Minist Educ, Key Lab Coal Gasificat & Energy Chem Engn, POB 272, Shanghai 200237, Peoples R China
[2] East China Univ Sci & Technol, Shanghai Engn Res Ctr Coal Gasificat, POB 272, Shanghai 200237, Peoples R China
基金
中国国家自然科学基金;
关键词
Particle swarm; Gasification; Coal char and petcoke; Particle temperature; Gasifying agent concentration; VICTORIAN BROWN-COAL; ENTRAINED-FLOW GASIFICATION; CO2; GASIFICATION; MASS-TRANSFER; KINETICS; BIOMASS; REACTIVITY; DIFFUSION; PREDICTION; PARAMETERS;
D O I
10.1016/j.fuel.2018.12.113
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this study, the effects of particle concentration on particle temperature and gasifying agent concentration was analyzed based on the gasification experiments. The gasification processes of different coal chars and petcoke were divided into fast reaction process (gasification of lignite and bituminous char) and slow reaction process (gasification of anthracite char and petcoke). The reactivity index of fast reactions was extremely higher than that of slow reactions. The reaction rate of sparse particle swarms also differed from that of dense particle swarms for the same sample. For fast reactions, the effects of particle concentration on gasification reactivity was limited. It was illustrated that the evident increase of particle temperature and the decrease of gasifying agent played a contrary effect on reactivity for fast-reaction samples. Nevertheless, the slight decrease of particle temperature and evident decrease of gasifying agent concentration led to the decrease of reaction rate with particle concentration for slow-reaction samples.
引用
收藏
页码:973 / 984
页数:12
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