An extended coal combustion model

被引:53
作者
Backreedy, RI [1 ]
Habib, R [1 ]
Jones, JM [1 ]
Pourkashanian, M [1 ]
Williams, A [1 ]
机构
[1] Univ Leeds, Dept Fuel & Energy, Leeds LS2 9JT, W Yorkshire, England
基金
英国工程与自然科学研究理事会;
关键词
bituminous coal; devolatilisation; combustion modelling;
D O I
10.1016/S0016-2361(99)00123-4
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
Current coal combustion models are a useful tool in research but they use simplified coal particle devolatilisation and combustion steps in order to meet computational limitations. The availability of more advanced computers enables the use of more detailed steps for devolatilisation and the use of more realistic char combustion processes. In the present work the devolatilisation rates were calculated using the coal devolatilisation model FG-DVC. In this way devolatilisation rates and the yields of char and volatile were obtained. A drop tube reactor was operated at 1623 K to collect char samples, from Thoresby coal, at different sampling positions or residence times, and proximate and ultimate analysis were conducted on these char samples to confirm the results. The detailed char combustion sub-models being developed for CFD codes require char properties such as densities, surface areas and pore size distributions but a simplified model was used here. In this case the use of a simple global char oxidation model together with an empirical derived 'volatile' and FG-DVC predicted devolatilisation rate data seem to give good agreement with the experimental results available for the char burnout. However, there still remains considerable uncertainty in the use of char burnout models including the one used here is not sufficiently accurate in predicting carbon burnout in all conditions. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:1745 / 1754
页数:10
相关论文
共 27 条
[1]   PREDICTING COMBUSTION BEHAVIOUR OF COAL PARTICLES [J].
BAUM, MM ;
STREET, PJ .
COMBUSTION SCIENCE AND TECHNOLOGY, 1971, 3 (05) :231-&
[2]  
Beeley T, 1996, TWENTY-SIXTH SYMPOSIUM (INTERNATIONAL) ON COMBUSTION, VOLS 1 AND 2, P3103
[3]   Modeling soot derived from pulverized coal [J].
Brown, AL ;
Fletcher, TH .
ENERGY & FUELS, 1998, 12 (04) :745-757
[4]  
CAHILL P, 1998, 30 PGB COAL RES EST
[5]  
CHARPENAY S, 1992, 24 S INT COMB COMB I, P1189
[6]   VARIATION OF CHAR REACTIVITY DURING SIMULTANEOUS DEVOLATILIZATION AND COMBUSTION OF COALS IN A DROP-TUBE REACTOR [J].
ELSAMED, AKA ;
HAMPARTSOUMIAN, E ;
FARAG, TM ;
WILLIAMS, A .
FUEL, 1990, 69 (08) :1029-1036
[7]  
*FLUENT INC, 1996, FLUENT US GUID, V2
[8]  
HAMPARTSOUMIAN E, 1989, J I ENERGY, P48
[9]  
Hargrave G., 1986, 21 S INT COMB COMB I, P221
[10]   A COMPARISON OF THE PYROLYSIS OF COAL IN WIRE-MESH AND ENTRAINED-FLOW REACTORS [J].
HINDMARSH, CJ ;
THOMAS, KM ;
WANG, WX ;
CAI, HY ;
GUELL, AJ ;
DUGWELL, DR ;
KANDIYOTI, R .
FUEL, 1995, 74 (08) :1185-1190