Product Distribution from Co-gasification of Coal and Biomass in a Fluidized-bed Reactor

被引:4
|
作者
Song, Y. -C. [1 ,2 ]
Ji, M. -S. [1 ,2 ]
Feng, J. [1 ,2 ]
Li, W. -Y. [1 ,2 ]
机构
[1] Taiyuan Univ Technol, Key Lab Coal Sci & Technol, Minist Educ & Shanxi Prov, Taiyuan 030024, Peoples R China
[2] Shanxi Prov & Minist Sci & Technol, Training Base State Key Lab Coal Sci & Technol, Taiyuan, Peoples R China
关键词
biomass; coal; co-gasification; fluidized-bed reactor; products distribution; WOODY BIOMASS; CATALYTIC GASIFICATION; SYNGAS PRODUCTION; TAR FORMATION; FIXED-BED; PYROLYSIS; CHAR; REACTIVITY; WASTES; AIR;
D O I
10.1080/15567036.2012.711798
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
Co-gasification of coal and biomass is an effective way to utilize coal of low rank to alleviate problems of energy shortage and environmental pollution. In order to investigate the product distribution resulting from the co-gasification of coal and biomass in a fluidized-bed reactor, experiments were conducted at varying biomass ratios, oxygen equivalent ratios, steam/carbon ratios, and also gasification temperatures. With an increase of biomass ratio, the amount of CO and CH4 increased while H-2 and CO2 contents decreased. The amount of H-2 increased obviously with an increase of gasification temperature ranging from 650 to 1000 degrees C, whereas the CO and CO2 amount decreased. An increase of the steam/carbon ratio was beneficial to promote H-2 formation and decrease CO and hydrocarbon compounds. With an increase of the gasification temperature, the steam/carbon ratio and oxygen equivalent ratio can promote the elements with low reaction activity in biomass gasification to be useful gas compositions.
引用
收藏
页码:2550 / 2558
页数:9
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