High temperature air-blown woody biomass gasification model for the estimation of an entrained down-flow gasifier

被引:36
作者
Kobayashi, Nobusuke [1 ]
Tanaka, Miku [1 ]
Piao, Guilin [1 ]
Kobayashi, Jun [2 ]
Hatano, Shigenobu [1 ]
Itaya, Yoshinori [1 ]
Mori, Shigekatsu [2 ]
机构
[1] Nagoya Univ, Dept Chem Engn, Nagoya, Aichi 4648603, Japan
[2] Nagoya Univ, Ctr Cooperat Res Adv Sci & Technol, Nagoya, Aichi 4648603, Japan
关键词
CIRCULATING FLUIDIZED-BED; EQUILIBRIUM-MODEL; POWER-GENERATION; WASTE GASIFIER; ELIMINATION; TECHNOLOGY; COMBUSTION; DOLOMITE; FUEL;
D O I
10.1016/j.wasman.2008.04.014
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A high temperature air-blown gasification model for woody biomass is developed based on an air-blown gasification experiment. A high temperature air-blown gasification experiment on woody biomass in an entrained down-flow gasifier is carried Out, and then the simple gasification model is developed based on the experimental results. In the experiment, air-blown gasification is conducted to demonstrate the behavior of this process. Pulverized wood is used as the gasification fuel, which is injected directly into the entrained down-flow gasifier by the pulverized wood banner. The pulverized wood is sieved through 60 mesh and supplied at rates of 19 and 27 kg/h. The oxygen-carbon molar ratio (O/C) is employed as the operational condition instead of the air ratio. The maximum temperature achievable is over 1400 K when the O/C is front 1.26 to 1.84. The results Show that the gas composition is followed by the CO-shift reaction equilibrium. Therefore, the air-blown gasification model is developed based on the CO-shift reaction equilibrium. The simple gasification model agrees well with the experimental results. From calculations in large-scale units, the cold gas is able to achieve 80% efficiency in the air-blown gasification, when the woody biomass feedrate is over 1000 kg/h and input air temperature is 700 K. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:245 / 251
页数:7
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