Gasification reactivity and kinetics of typical chinese anthracite chars with steam and CO2

被引:112
作者
Zhang, LX [1 ]
Huang, JJ
Fang, YT
Wang, Y
机构
[1] Chinese Acad Sci, Inst Coal Chem, Taiyuan 030001, Peoples R China
[2] Chinese Acad Sci, Grad Sch, Beijing 100039, Peoples R China
关键词
D O I
10.1021/ef050343o
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 gasification reactivities of six typical Chinese anthracite chars with steam and CO2 at 0.02-0.1 MPa and 920-1050 degrees C were investigated by using thermogravimetric analysis (TGA). The reactivities of anthracite chars during steam gasification were found to have a good correlation to the coal volatile matter contents. The higher the coal volatile matter content, the higher the reactivity. The difference in reactivities of anthracite chars during CO2 gasification seems to be more dependent on the catalytic effect of inherent minerals in anthracite. The results show that the greater the alkali index, the higher the reactivity. The reactivities of demineralized anthracite chars vary very little compared with those the undemineralized chars at higher temperatures, whereas the reactivities of demineralized chars from Jincheng and Rujigou are lower than those of undemineralized ones and the reactivities of demineralized chars from Yangquan, Hunan, Guangdong, and Longyan are higher than those of undemineralized chars at lower temperatures. The homogeneous model and shrinking core model were examined as ways to interpret the experimental data. The experimental results could be well-described by the shrinking core model for anthracite chars during steam and CO2 gasification. Comparison of the reactivities for anthracite chars during steam and CO2 gasification shows that the reactivities of anthracite chars during steam gasification are far higher than those during CO2 gasification. The reactivities of the former are about 10 times higher than those of the latter, and this ratio is far greater than that of the lignite and bituminous coal. The mechanism leading to this difference is discussed.
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页码:1201 / 1210
页数:10
相关论文
共 34 条
[1]   MINERAL MATTER EFFECTS ON THE REACTIVITY OF CHARS DURING GASIFICATION [J].
ADANEZ, J ;
DEDIEGO, LF .
FUEL PROCESSING TECHNOLOGY, 1990, 24 :298-304
[2]   REACTIVITY OF COAL AND CHAR .1. CARBON-DIOXIDE ATMOSPHERE [J].
DUTTA, S ;
WEN, CY ;
BELT, RJ .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (01) :20-30
[3]  
FUJITA H, 1982, J FUEL SOC JPN, V61, P301
[4]   NATURE OF POROSITY IN AMERICAN COALS [J].
GAN, H ;
WALKER, PL ;
NANDI, SP .
FUEL, 1972, 51 (04) :272-&
[5]   GASIFICATION KINETICS OF WESTERN KENTUCKY BITUMINOUS COAL CHAR [J].
GOYAL, A ;
ZABRANSKY, RF ;
REHMAT, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1989, 28 (12) :1767-1778
[6]  
GUO CT, 1994, COAL CHEM M, P47
[7]  
HASHIMOTO K, 1984, RES COAL LIQUEFACTIO, P229
[8]   REACTIVITY OF HEAT-TREATED COALS IN CARBON-DIOXIDE AT 900 DEGREESC [J].
HIPPO, E ;
WALKER, PL .
FUEL, 1975, 54 (04) :245-248
[9]   THE ROLE OF MICROPOROUS SURFACE-AREA IN THE GASIFICATION OF CHARS FROM A SUB-BITUMINOUS COAL [J].
HURT, RH ;
SAROFIM, AF ;
LONGWELL, JP .
FUEL, 1991, 70 (09) :1079-1082
[10]  
JOHNSON JL, 1979, KINETICS COAL GASIFI, P283