The design and operation of a new clapboard-type internal circulating fluidized-bed gasifier

被引:1
作者
Ma, L. -L. [1 ,2 ]
Yan, Y. -J. [2 ]
Wu, C. -Z. [1 ]
Li, T. -C. [2 ]
Marzetti, P. [3 ]
Scoditti, E. [3 ]
Braccio, G. [4 ]
机构
[1] Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou, Guangdong, Peoples R China
[2] E China Univ Sci & Technol, Shanghai 200237, Peoples R China
[3] ENEA, CASACCIA Res Ctr, Rome, Italy
[4] ENEA, TRISAIA Res Ctr, Rome, Italy
关键词
biomass gasification; clapboard-type internal circulating fluidized-bed gasifier; design and operation;
D O I
10.1080/15567030701258329
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
The design and operation of a new clapboard-type internal circulating fluidized-bed gasifier is proposed in this article. By arranging the clapboard in the bed, the gasifier is thus divided into two regions, which are characterized by different fluidization velocities. The bed structure is designed so that it can guide the circulating flow passing through the two regions, and therefore the feedstock particles entrained in the flow experience longer residence time. The experimental results based on the present new design, operating in the temperature range of 790 degrees C-850 degrees C, indicate that the gas yield is from 1.6-1.9 Nm(3)/kg feedstock, the gas enthalpies are 5,345 kJ/Nm(3) for wood chip and 4,875 kJ/m(3) for rice husk, and a gasification efficiency up to 75% can be obtained.
引用
收藏
页码:1563 / 1571
页数:9
相关论文
共 15 条
[1]   Catalytic hot gas cleaning with monoliths in biomass gasification in fluidized beds. 1. Their effectiveness for tar elimination [J].
Corella, J ;
Toledo, M ;
Padilla, R .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (10) :2433-2445
[2]   Biomass gasification in fluidized bed: Where to locate the dolomite to improve gasification? [J].
Corella, J ;
Aznar, MP ;
Gil, J ;
Caballero, MA .
ENERGY & FUELS, 1999, 13 (06) :1122-1127
[3]  
DAIZO K, 1997, CHEM ENG SCI, V52, P2471
[4]   A review of the primary measures for tar elimination in biomass gasification processes [J].
Devi, L ;
Ptasinski, KJ ;
Janssen, FJJG .
BIOMASS & BIOENERGY, 2003, 24 (02) :125-140
[5]  
JAVIER G, 1999, BIOMASS BIOENERG, V17, P389
[6]   The UNDP/World Bank monitoring program on small scale biomass gasifiers (BTG's experience on tar measurements) [J].
Knoef, HAM .
BIOMASS & BIOENERGY, 2000, 18 (01) :39-54
[7]   Formation of NOx and SOx precursors during the pyrolysis of coal and biomass.: Part III.: Further discussion on the formation of HCN and NH3 during pyrolysis [J].
Li, CZ ;
Tan, LL .
FUEL, 2000, 79 (15) :1899-1906
[8]  
LU PM, 2003, ENERG FUEL, V3, P677
[9]  
PALZ W, 1981, ENERGY BIOMASS
[10]   Circulation of solids and gas bypassing in an internally circulating fluidized bed with a draft tube [J].
Song, BH ;
Kim, YT ;
Kim, SD .
CHEMICAL ENGINEERING JOURNAL, 1997, 68 (2-3) :115-122