Investigation of Coal Char-Slag Transition during Oxidation: Effect of Temperature and Residual Carbon

被引:32
作者
Li, Suhui [1 ]
Whitty, Kevin J. [1 ]
机构
[1] Univ Utah, Inst Clean & Secure Energy, Salt Lake City, UT 84112 USA
关键词
KINETICALLY CONTROLLED CONDITIONS; FLUID-SOLID REACTIONS; HIGHLY POROUS CHARS; RANDOM PORE MODEL; PULVERIZED-COAL; ASH DEPOSITION; GASIFICATION; COMBUSTION;
D O I
10.1021/ef801082j
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 transition of coal char to molten slag at high conversion was studied for a bituminous coal using a laminar entrained-flow reactor under oxidizing conditions. Post-oxidized char particles were analyzed by various techniques including loss-on-ignition, gas adsorption analysis, and scanning electron microscopy to determine carbon content, internal surface area and pore size distribution, and char morphology, respectively. These analyses provide information concerning the effect of temperature and residual carbon on the transition from porous char to molten slag. Results showed that, at temperatures above the ash flow temperature, the transition from porous char to molten slag occurred at about 90% conversion for the coal used in this study. No transition occurred at temperatures below the ash flow temperature. This finding explains previous observations that there is a coal-dependent critical carbon conversion at which the ash stickiness increases dramatically. This result also indicates that surface area can be used as a criterion for determining the critical conversion of the transition. In addition, it was found that the randomly overlapping pore model cannot be directly applied to predict the surface area evolution of char particles during the transition without considering the reopening of closed micropores during the initial reaction and the ash fusion effect.
引用
收藏
页码:1998 / 2005
页数:8
相关论文
共 32 条
[1]   Mutual effects of porosity and reactivity in char oxidation [J].
Bar-Ziv, E ;
Kantorovich, II .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2001, 27 (06) :667-697
[2]   Study of coal ash deposition in an entrained flow reactor:: Influence of coal type, blend composition and operating conditions [J].
Barroso, J. ;
Ballester, J. ;
Ferrer, L. M. ;
Jiménez, S. .
FUEL PROCESSING TECHNOLOGY, 2006, 87 (08) :737-752
[3]   CHAR FRAGMENTATION AND FLY-ASH FORMATION DURING PULVERIZED-COAL COMBUSTION [J].
BAXTER, LL .
COMBUSTION AND FLAME, 1992, 90 (02) :174-184
[4]   ASH DEPOSITION DURING BIOMASS AND COAL COMBUSTION - A MECHANISTIC APPROACH [J].
BAXTER, LL .
BIOMASS & BIOENERGY, 1993, 4 (02) :85-102
[5]   A MECHANISTIC DESCRIPTION OF ASH DEPOSITION DURING PULVERIZED COAL COMBUSTION - PREDICTIONS COMPARED WITH OBSERVATIONS [J].
BAXTER, LL ;
DESOLLAR, RW .
FUEL, 1993, 72 (10) :1411-1418
[6]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[7]   A RANDOM PORE MODEL FOR FLUID-SOLID REACTIONS .2. DIFFUSION AND TRANSPORT EFFECTS [J].
BHATIA, SK ;
PERLMUTTER, DD .
AICHE JOURNAL, 1981, 27 (02) :247-254
[8]  
Bool L.E., 1995, ASME ENV CONTROL DIV, V20, P305
[9]   Variation of the pore structure of coal chars during gasification [J].
Feng, B ;
Bhatia, SK .
CARBON, 2003, 41 (03) :507-523
[10]   A RANDOM CAPILLARY MODEL WITH APPLICATION TO CHAR GASIFICATION AT CHEMICALLY CONTROLLED RATES [J].
GAVALAS, GR .
AICHE JOURNAL, 1980, 26 (04) :577-585