Operating condition optimization of biomass microgasification for syngas production

被引:0
|
作者
Ahumada L.M. [1 ]
Verdeza A. [1 ]
Bula A.J. [1 ]
Lombana J. [1 ]
机构
[1] Facultad de Ingeniería, Dpto. de Ingeniería Mecánica, Univ. del Norte, Barranquilla
来源
| 1600年 / Centro de Informacion Tecnologica卷 / 27期
关键词
Biomass gasification; Calorific value; Optimization; Syngas; Thermochemical conversion;
D O I
10.4067/S0718-07642016000300017
中图分类号
学科分类号
摘要
The results of study on the significance and the optimization of some variables (particle size, air flow, biomass content and reactor disposition) in the calorific value of the synthesis gas obtained by gasification process of biomass (vegetal coal and biomass African palm) is presented. The four variables ranged from 8-13mm for the particle size, 0.8-1.4m/s for air flow, 0-100 for biomass content and updraft-downdraft disposition for the type of reactor were evaluated by an experimental design. It was found that the particle size and biomass content are the most significant factors to maximize the output calorific value of syngas. A maximum calorific value of 3.84MJ/Nm3 was obtained using the downdraft reactor with 13mm particle size and maximum air flow supply. The verification of the optimum operating point under these conditions showed that such operating conditions favored the production of a gas with high calorific value.
引用
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页码:179 / 188
页数:9
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