A STUDY OF THE CO2-O2 COAL-GASIFICATION PROCESS

被引:2
|
作者
ALFANTAZI, AM
PICKLES, CA
机构
[1] Department of Materials and Metallurgical Engineering, Queen’s University, Kingston, ON
基金
加拿大自然科学与工程研究理事会;
关键词
COAL GASIFICATION; FIXED BED; BOUDOUARD REACTION; GAS CHROMATOGRAPHY; CARBON DIOXIDE; OXYGEN; COAL;
D O I
10.1080/09603409.1992.11689398
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
In this work, a fixed-bed gasifier was used to study the effects of some important parameters on both the temperature and the chemical composition of the off-gas produced in a CO2-O2 coal gasification process. Also, the effect of these parameters on the gasification temperature was determined. The parameters tested included input-gas composition, coal rank, coal size and coal-bed depth. In addition, the reactivity of a sub-bituminous coal was investigated under different gasification temperatures. Gas chromatography was employed to analyse the chemical composition of the gases. The results indicated that the off-gas temperature increased with coal rank and decreased with both the CO2-O2 ratio and the coal-bed depth. Generally, the amount of H-2 and CO in the off-gas decreased with both the coal rank and the CO2-O2 ratio and increased with coal-bed depth. Coal size did not have a significant effect on the gasification process.
引用
收藏
页码:51 / 59
页数:9
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