Experimental study on air-stream gasification of biomass micron fuel (BMF) in a cyclone gasifier

被引:37
作者
Guo, X. J. [1 ,2 ]
Xiao, B. [2 ]
Zhang, X. L. [1 ]
Luo, S. Y. [2 ]
He, M. Y. [2 ]
机构
[1] Yantai Univ, Sch Environm & Mat Engn, Yantai 264005, Peoples R China
[2] Huazhong Univ Sci & Technol, Sch Environm Sci & Engn, Wuhan 430074, Peoples R China
关键词
Biomass micron fuel (BMF); Cyclone gasifier; Air-stream gasification; HYDROGEN-RICH GAS; STEAM-GASIFICATION; FLUIDIZED-BED; PYROLYSIS; REACTOR;
D O I
10.1016/j.biortech.2008.07.007
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Based on biomass micron fuel (BMF) with particle size of less than 250 mu m, a cyclone gasifier concept has been considered in our laboratory for biomass gasification. The concept combines and integrates partial oxidation, fast pyrolysis, gasification, and tar cracking, as well as a shift reaction, with the purpose of producing a high quality of gas. In this paper, experiments of BMF air-stream gasification were carried out by the gasifier, with energy for BMF gasification produced by partial combustion of BMF within the gasifier using a hypostoichiometric amount of air. The effects of ER (0.22-0.37) and S/B (0.15-0.59) and biomass particle size on the performances of BMF gasification and the gasification temperature were studied. Under the experimental conditions, the temperature. gas yields, LHV of the gas fuel, carbon conversion efficiency, stream decomposition and gasification efficiency varied in the range of 586-845 degrees C, 1.42-2.21 N m(3)/kg biomass, 3806-4921 kJ/m(3), 54.44%-85.45%, 37.98%-70.72%, and 36.35%-56.55%, respectively. The experimental results showed that the gasification performance was best with ER being 3.7 and S/B being 0.31 and smaller particle, as well as H-2-content. And the BMF gasification by air and low temperature stream in the cyclone gasifier with the energy self-sufficiency is reliable. (c) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1003 / 1006
页数:4
相关论文
共 18 条
[1]   A novel biomass air gasification process for producing tar-free higher heating value fuel gas [J].
Cao, Y ;
Wang, Y ;
Riley, JT ;
Pan, WP .
FUEL PROCESSING TECHNOLOGY, 2006, 87 (04) :343-353
[2]   Biomass gasification integrated with pyrolysis in a circulating fluidised bed [J].
Chen, G ;
Andries, J ;
Spliethoff, H ;
Fang, M .
SOLAR ENERGY, 2004, 76 (1-3) :345-349
[3]   140gH2/kg biomass d.a.f. by a CO-shift reactor downstream from a FB biomass gasifier and a catalytic steam reformer [J].
Corell, Jose ;
Aznar, Maria P. ;
Caballero, Miguel A. ;
Molina, Gregorio ;
Toledo, Jos M. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (07) :1820-1826
[4]   Development of Ni catalysts for gas production from biomass gasification. Reactivity in steam- and dry-reforming [J].
Courson, C ;
Makaga, E ;
Petit, C ;
Kiennemann, A .
CATALYSIS TODAY, 2000, 63 (2-4) :427-437
[5]   Kinetic and heat transfer control in the slow and flash pyrolysis of solids [J].
DiBlasi, C .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1996, 35 (01) :37-46
[6]   Hydrogen production from biomass coupled with carbon dioxide capture: The implications of thermodynamic equilibrium [J].
Florin, Nicholas H. ;
Harris, Andrew T. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (17) :4119-4134
[7]   Biomass gasification in atmospheric and bubbling fluidized bed: Effect of the type of gasifying agent on the product distribution [J].
Gil, J ;
Corella, J ;
Aznar, MP ;
Caballero, MA .
BIOMASS & BIOENERGY, 1999, 17 (05) :389-403
[8]  
GUO XJ, 2008, FRESEN ENVIRON BULL, V17, P310
[9]   The design, construction and operation of a 75 kW two-stage gasifier [J].
Henriksen, Ulrik ;
Ahrenfeldt, Jesper ;
Jensen, Torben Kvist ;
Gobel, Benny ;
Bentzen, Jens Dall ;
Hindsgaul, Claus ;
Sorensen, Lasse Holst .
ENERGY, 2006, 31 (10-11) :1542-1553
[10]  
[赖艳华 Lai Yanhua], 2002, [燃烧科学与技术, Journal of combustion science and technology], V8, P478