A study of the CO2−O2coal gasification process
- 1 February 1992
- journal article
- research article
- Published by Taylor & Francis in Materials at High Temperatures
- Vol. 10 (1) , 51-59
- https://doi.org/10.1080/09603409.1992.11689398
Abstract
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 H2 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.Keywords
This publication has 7 references indexed in Scilit:
- Steam gasification of Mississippi Lignite in a fixed bed gasifierFuel Processing Technology, 1988
- Laboratory gasification study of Canadian coals: 2. Chemical reactivity and coal rankFuel, 1983
- Coal gasification at pressure by mixtures of carbon dioxide and oxygenFuel, 1983
- Laboratory gasification of five Canadian coalsFuel, 1982
- Reactivities of carbon to steam and hydrogen and applications to technical gasification processes—A reviewCarbon, 1981
- Rapid devolatilization and hydrogasification of bituminous coalFuel, 1976
- Reactivity of heat-treated coals in air at 500 °CFuel, 1973