共 25 条
Four Zones Modeling of the Downdraft Biomass Gasification Process: Effects of moisture content and air to fuel ratio
被引:34
作者:
Dejtrakulwong, C.
[1
]
Patumsawad, S.
[2
]
机构:
[1] King Mongkuts Univ Technol Thonburi, Joint Grad Sch Energy & Environm, Bangkok, Thailand
[2] King Mongkuts Univ Technol N Bangkok, Fac Engn, Dept Mech Engn, Bangkok, Thailand
来源:
2013 INTERNATIONAL CONFERENCE ON ALTERNATIVE ENERGY IN DEVELOPING COUNTRIES AND EMERGING ECONOMIES (2013 AEDCEE)
|
2014年
/
52卷
关键词:
Gasification;
Modeling;
Biomass;
Downdraft gasifier;
Synthesis gas;
FIXED-BED;
EQUILIBRIUM-MODEL;
WASTE GASIFIER;
PYROLYSIS;
CHAR;
PREDICTION;
PARTICLE;
WOOD;
PERFORMANCE;
PARAMETERS;
D O I:
10.1016/j.egypro.2014.07.064
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 mathematical model of a biomass downdraft gasification process has been developed. The model was considered to be four modules that are drying, pyrolysis, oxidation, and reduction which the products of upper module will be the reactants of the next. The one-dimensional kinetic finite rate models were applied to drying and reduction modules. The pyrolysis model took place when drying temperature reached 473 K. The equilibrium sequence model was used to describe the oxidation process by considering the sequence of order of reaction rates. For the model validation the comparison showed a good agreement. In the parametric study the moisture content increasing affected the height of drying, and pyrolysis zones increasing while the critical char bed length of reduction zone decreased from 0.53 to 0.25 m. The height of these zones decreased along A/F increasing. The results of this study can be used in the reactor design evaluation. (C) 2014 Published by Elsevier Ltd.
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页码:142 / 149
页数:8
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