MODIFICATION OF A FLUIDIZED-BED COAL-GASIFICATION PROCESS TO IMPROVE CARBON CONVERSION

被引:0
|
作者
GALE, JJ
LAUGHLIN, KM
LANE, GJ
机构
来源
JOURNAL OF THE INSTITUTE OF ENERGY | 1991年 / 64卷 / 460期
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暂无
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
A spouted fluidised-bed coal-gasification process has been developed by the British Coal Corporation for the manufacture of a fuel gas of low calorific value (4.0 MJ m-3 gross) for use in industrial applications. During the initial development work the carbon-conversion efficiency of the process was restricted to 65%. The process has now been modified successfully by the substitution of bauxite for the original char bed. When the gasifier bed is operated in this way, a bed with a low carbon content is maintained; this has led to significantly reduced elutriation rates, which have allowed carbon conversion efficiencies of the order of 85% to be achieved.
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页码:143 / 150
页数:8
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