Modeling of biomass gasification in fluidized bed

被引:688
作者
Gomez-Barea, A. [1 ]
Leckner, B. [2 ]
机构
[1] Univ Seville, Escuela Super Ingenieros, Chem & Environm Engn Dept, Bioenergy Grp, Seville 41092, Spain
[2] Chalmers Univ Technol, Environm & Energy Dept, S-41296 Gothenburg, Sweden
关键词
Gasification; Fluidized bed; Modeling; Fluidization; Simulation; Review; PINE WOOD PARTICLES; RICE HUSK GASIFIER; COAL DEVOLATILIZATION KINETICS; UPPER DILUTE ZONE; OF-THE-ART; STEAM-GASIFICATION; SINGLE-PARTICLE; MATHEMATICAL-MODEL; CHAR GASIFICATION; FLASH PYROLYSIS;
D O I
10.1016/j.pecs.2009.12.002
中图分类号
O414.1 [热力学];
学科分类号
摘要
Modeling of biomass gasification in bubbling and circulating fluidized bed (FB) gasifiers is reviewed. Approaches applied for reactor modeling, from black-box models to computational fluid-dynamic models, are described. Special attention is paid to comprehensive fluidization models, where semi-empirical correlations are used to simplify the fluid-dynamics. The conversion of single fuel particles, char, and gas is examined in detail. The most relevant phenomena to be considered in modeling of FB biomass gasifiers are outlined, and the need for further investigation is identified. An updated survey of published mathematical reactor models for biomass and waste gasification in FB is presented. The overall conclusion is that most of the FB biomass gasification models fit reasonably well experiments selected for validation, despite the various formulations and input data. However, there are few measurements available for comparison with detailed model results. Also, validation of models with data from full-scale FB biomass gasification units remains to be done. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:444 / 509
页数:66
相关论文
共 395 条
[1]   Review of catalysts for tar elimination in Biomass gasification processes [J].
Abu El-Rub, Z ;
Bramer, EA ;
Brem, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (22) :6911-6919
[2]   Combustion of wood chips in a CFBC.: Modeling and validation [J].
Adánez, J ;
Gayán, P ;
de Diego, LF ;
García-Labiano, F ;
Abad, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (05) :987-999
[3]   PREDICTION OF CO2 GASIFICATION RATE OF CHAR IN FLUIDIZED-BED GASIFIER [J].
ADSCHIRI, T ;
SHIRAHA, T ;
KOJIMA, T ;
FURUSAWA, T .
FUEL, 1986, 65 (12) :1688-1693
[4]  
AGARWAL PK, 1989, CHEM ENG RES DES, V67, P457
[5]   COUPLED DRYING AND DEVOLATILIZATION OF WET COAL IN FLUIDIZED-BEDS [J].
AGARWAL, PK ;
GENETTI, WE ;
LEE, YY .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (09) :2373-2383
[6]   INTERACTIVE PROCESSES IN GASIFICATION AND COMBUSTION .2. ISOLATED CARBON, COAL AND POROUS CHAR PARTICLES [J].
ANNAMALAI, K ;
RYAN, W .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 1993, 19 (05) :383-446
[7]  
[Anonymous], P 10 S INT COMB COMB
[8]  
[Anonymous], 1978, ENERGIYA
[9]  
[Anonymous], 2005, THESIS CHALMERS U TE
[10]  
[Anonymous], P COMBUSTION I