X-ray diffraction parameters and reaction rate modeling for gasification and combustion of chars derived from inertinite-rich coals

被引:66
作者
Everson, Raymond C. [1 ]
Okolo, Gregory N. [1 ]
Neomagus, Hein W. J. P. [1 ]
dos Santos, Jaen-Mari [1 ]
机构
[1] North West Univ, Sch Chem & Minerals Engn, Unit Energy Syst, Coal Res Grp, ZA-2520 Potchefstroom, South Africa
关键词
Inertinite-rich coals; Devolitalization; Gasification and combustion reactivity; X-ray diffraction properties; Intrinsic reaction rates; CO2; GASIFICATION; KINETIC-ANALYSIS; HEAT-TREATMENT; GRAPHITIZATION; EVOLUTION; XRD;
D O I
10.1016/j.fuel.2012.12.043
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
An investigation was undertaken to determine the effect of carbon structural properties on the reactivity of chars derived from inertinite-rich coal. The structures of chars were characterized by X-ray diffraction and the reactivity evaluation with respect to gasification and combustion involving experimentation and reaction rate modeling was carried out. The effect of the aromaticity on the intrinsic reaction rates and associated activation energy for gasification and combustion of chars were determined based on chemical reaction rate controlled kinetics. Two sets of results were examined consisting of gasification with four char samples derived from different inertinite-rich coals prepared with a devolitalization temperature of 900 degrees C (Set 1) and three chars from the same parent coal also rich in inertinites prepared at different devolitalization temperatures, namely 550, 700 and 850 degrees C (Set 2). It was found that the aromaticity and fraction of crystalline carbon of the four chars prepared at the same temperature (Set 1) varied in the ranges 0.85-0.95 and 0.52-0.72 respectively and the chars prepared at different temperatures (Set 2) in the ranges 0.82-0.92 and 0.44-0.74 respectively. The structural properties of the chars within each set of results were also very different which required reaction rate modeling for the determination of intrinsic reactivities. The random pore model with chemical reaction controlling described the reaction kinetics accurately and it was found that the intrinsic reactivity of the char decreased with increasing aromaticity while the activation energies decreased (aromaticity < 0.92) which indicated the effect of the variation of the distribution of aromatic/aliphatic structures on the intrinsic reaction rate. It is proposed that the aromaticity of chars be used as a predictive index for char reactivity under chemical reaction controlled conditions. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:148 / 156
页数:9
相关论文
共 30 条
[21]   Microstructural changes and loss of gasification reactivity of chars upon heat treatment [J].
Senneca, O ;
Salatino, P ;
Masi, S .
FUEL, 1998, 77 (13) :1483-1493
[22]   A simple kinetic analysis to determine the intrinsic reactivity of coal chars [J].
Sima-Ella, E ;
Yuan, G ;
Mays, T .
FUEL, 2005, 84 (14-15) :1920-1925
[23]   Changes to the organic functional groups of an inertinite rich medium rank bituminous coal during acid treatment processes [J].
Strydom, C. A. ;
Bunt, J. R. ;
Schobert, H. H. ;
Raghoo, M. .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (04) :764-770
[24]   A proposed maceral index to predict combustion behavior of coal [J].
Su, S ;
Pohl, JH ;
Holcombe, D ;
Hart, JA .
FUEL, 2001, 80 (05) :699-706
[25]   XRD analysis of carbon stacking structure in coal during heat treatment [J].
Takagi, H ;
Maruyama, K ;
Yoshizawa, N ;
Yamada, Y ;
Sato, Y .
FUEL, 2004, 83 (17-18) :2427-2433
[26]   Characterization of asphaltenes from hydrotreated products by SEC, LDMS, MALDI, NMR, and XRD [J].
Trejo, F. ;
Ancheyta, J. ;
Morgan, T. J. ;
Herod, A. A. ;
Kandiyoti, R. .
ENERGY & FUELS, 2007, 21 (04) :2121-2128
[27]  
Webb P.A., 2001, Volume and Density Determinations for Particle Technologists
[28]   Variation of carbon crystalline structures and CO2 gasification reactivity of Shenfu coal chars at elevated temperatures [J].
Wu, Shiyong ;
Gu, Jing ;
Zhang, Xiao ;
Wu, Youqing ;
Gao, Jinsheng .
ENERGY & FUELS, 2008, 22 (01) :199-206
[29]   Gasification reactivity and kinetics of typical chinese anthracite chars with steam and CO2 [J].
Zhang, LX ;
Huang, JJ ;
Fang, YT ;
Wang, Y .
ENERGY & FUELS, 2006, 20 (03) :1201-1210
[30]   A comparison of coal char reactivity determined from thermogravimetric and laminar flow reactor experiments [J].
Zolin, A ;
Jensen, A ;
Pedersen, LS ;
Dam-Johansen, K ;
Torslev, P .
ENERGY & FUELS, 1998, 12 (02) :268-276