Circulating fluidised bed co-combustion of coal and biomass

被引:73
作者
Gayan, P
Adanez, J
de Diego, LF
García-Labiano, F
Cabanillas, A
Bahillo, A
Aho, M
Veijonen, K
机构
[1] CSIC, Inst Carboquim, Zaragoza 50015, Spain
[2] CIEMAT, E-28040 Madrid, Spain
[3] VTT Energy, Jyvaskyla, Finland
关键词
co-firing; circulating fluidised beds; mathematical modelling;
D O I
10.1016/j.fuel.2003.08.003
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
Circulating fluidised bed combustion (CFBC) is receiving wide research attention in view its potential as an economic and environmentally acceptable technology for burning low-grade coals, biomass and organic wastes, and thereby mixtures of them. Designs of the existing fluidised bed boilers for biomass combustion are mainly based on experience from coal combustion because the mechanism of combustion of biomass in fluidised beds is still not well understood. A good understanding of the combustion and pollutant formation processes and the modelling of the combustor can greatly avoid costly upsets of the plants. In this paper, the performance of CFBC burning coal and biomass mixtures was analysed. Experimental results were obtained from the combustion of two kinds of coal with a forest residue (Pine bark) in two CFB pilot plants (0.1 and 0.3 MWth). The effect of the main operating conditions on carbon combustion efficiency was analysed. Moreover, a mathematical model to predict the behaviour of the co-combustion of coal and biomass wastes in CFB boilers has been developed and validated. The developed model can predict the different gas concentrations along the riser (O-2, CO, CH4, etc.), and the carbon combustion efficiency. The experimental results of carbon combustion efficiencies were compared with those predicted by the model and a good correlation was found for all the conditions used. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:277 / 286
页数:10
相关论文
共 30 条
[1]   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
[2]   EFFECT OF FORMULATION OF STEADY-STATE HEAT-BALANCE FOR CHAR PARTICLES ON AFBC MODELING [J].
ADANEZ, J ;
ABANADES, JC ;
GAYAN, P .
FUEL, 1993, 72 (09) :1335-1342
[3]   A MODEL FOR PREDICTION OF CARBON COMBUSTION EFFICIENCY IN CIRCULATING FLUIDIZED-BED COMBUSTORS [J].
ADANEZ, J ;
DEDIEGO, LF ;
GAYAN, P ;
ARMESTO, L ;
CABANILLAS, A .
FUEL, 1995, 74 (07) :1049-1056
[4]  
ADANEZ J, 2002, 7220PR074 ECSC CSIC
[5]  
AMAND L, 2001, P 16 INT C FBC NEW Y
[6]  
[Anonymous], P 14 INT C FLUID BED
[7]   Co-combustion of coal and olive oil industry residues in fluidised bed [J].
Armesto, L ;
Bahillo, A ;
Cabanillas, A ;
Veijonen, K ;
Otero, J ;
Plumed, A ;
Salvador, L .
FUEL, 2003, 82 (08) :993-1000
[8]  
CHAKRABORTY RK, 1981, J I ENERGY, V54, P48
[9]   Effect of coal minerals on chlorine and alkali metals released during biomass/coal cofiring [J].
Dayton, DC ;
Belle-Oudry, D ;
Nordin, A .
ENERGY & FUELS, 1999, 13 (06) :1203-1211
[10]   Modeling of the devolatilization of nonspherical wet pine wood particles in fluidized beds [J].
de Diego, LF ;
García-Labiano, F ;
Abad, A ;
Gayán, P ;
Adánez, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (15) :3642-3650