scholarly journals The Design and Operation of a New Clapboard-Type Internal Circulating Fluidized-Bed Gasifier

Author(s):  
Zhengshun Wu ◽  
Chuanfang Zhu ◽  
Long-Long Ma ◽  
Chuangzhi Wu

The design and operation of a new clapboard-type Internal Circulating Fluidized-Bed gasifier is introduced in this paper. By setting clapboard in the middle of gasifier, bed layer in gasifier is divided into two regions that have different fluidization velocity, the incompletely reacted fuel or carbon in the high velocity region flows to the low velocity region companying with bed medium, and gasification reaction takes place in this region; still incompletely reacted fuel or carbon returns to the high velocity region in the bottom of gasifier, then gasification reaction further occurs. By this way, internal circulation in the gasifier was formed, gasification reaction time and efficiency increased. The experimental results indicate that gas yield (1.6 ∼ 1.9Nm3/kg fuel), gas heat values (5340kJ/Nm3 for wood chip fuel and 4880kJ/m3 for rice husk), and gasification efficiency (70%) can be obtained using this kind of gasifier in the optimal operational temperature range of 790∼850°C.

Author(s):  
Xianan Xiang ◽  
Guangcai Gong ◽  
Chenhua Wang ◽  
Ninghua Cai ◽  
Kun Tang ◽  
...  

Abstract The triple-bed circulating fluidized bed gasifier is a new type of the gasification process in which the combustion process, pyrolysis process, and gasification process of the fuel are carried out in different reactors. The inert heat carrier is used to transfer heat between the reactors. In this way, the gasification efficiency of char is improved since the tar and pyrolysis gas generated in the pyrolysis process will no longer hinder the gasification of the char. The thermodynamic equilibrium model is used to simulate the gasification process of the triple-bed circulating fluidized bed, and the sub-models are established to simulate combustion, pyrolysis, and gasification processes. The simulation results agree well with the experimental values. Besides, the model studies the effects of key parameters such as the gasification reaction temperature and the ratio of steam to C (S/C) on gasification performance. Results showed that higher gasification reaction temperature has a positive effect on gasification performance, S/C may not be too high, and excessive water vapor will directly affect the gasification reaction.


Energy ◽  
2020 ◽  
Vol 192 ◽  
pp. 116682 ◽  
Author(s):  
Debarshi Mallick ◽  
Pinakeswar Mahanta ◽  
Vijayanand S. Moholkar

1992 ◽  
Vol 3 (2) ◽  
pp. 105-110 ◽  
Author(s):  
Wu Jianzhi ◽  
Xu Bingyan ◽  
Lou Zhenfang ◽  
Zhou Xiguang

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