Gasification and char combustion reactivities of Daw Mill coal in wire-mesh and 'hot-rod' reactors

被引:30
作者
Lim, JY
Chatzakis, IN
Megaritis, A
Cai, HY
Dugwell, DR
Kandiyoti, R
机构
[1] Dept. Chem. Eng. and Chem. Technol., Imperial College
关键词
coal gasification; char reactivity; N and S partitioning;
D O I
10.1016/S0016-2361(97)00029-X
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 pyrolysis and CO2-gasification behaviour of Daw Mill (UK) coal was investigated using wire-mesh (WMR) and fixed-bed 'hot-rod' (HRR) reactors. Experiments were performed at pressures between 0.1 and 3 MPa at 850 and 1000 degrees C. These reaction conditions reflect those of novel power plant technologies (e.g. ABGC) in which coal gasification and char combustion reactivities are relevant to design and operation. Untreated coal samples were used in all experiments rather than pre-prepared chars as appears more usual. CO2 gasification reaction rates were directly calculated from the difference between mass loss in pyrolysis and during gasification in CO2. Combustion reactivities of the chars from these experiments were determined in an atmospheric pressure thermogravimetric balance. The partitioning of the original sulfur and nitrogen contents between the volatiles released in the gasifier and the char transferred for combustion in the CFBC were determined. Differences in mass loss between gasification and inert pyrolysis were found to be significantly greater in the wire-mesh reactor, where more efficient gas-solid contact takes place and tar condensation on reacting char is minimized. Whilst combustion reactivities of the CO2-gasification chars were lower than their pyrolysis counterparts and tended to decline slightly with increasing pressure, reactivities of chars prepared in the HRR were systematically lower than those from the WMR. The reactivities of four other coals were also tested at 1000 degrees C and 2 MPa. A straightforward decline in pyrolysis mass loss was found with increasing rank. However, even within the limits of the small number of samples tested, considerable scatter was found in the reactivities of middle-rank coals, probably due to a combination of structural factors, including differences in char pore structure, catalytic effects of mineral matter components and differences in the inherent reactivity of the carbonaceous matter. The percentages of coal nitrogen and sulfur retained in the residual chars generally declined with increasing pressure; reactive gases appear to remove char nitrogen more efficiently, suggesting that pyrolysis experiments may not be a good guide to char nitrogen partitioning in gasification and combustion. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:1327 / 1335
页数:9
相关论文
共 18 条
[1]   INFLUENCE OF CARRIER GAS-FLOW AND HEATING RATES IN FIXED-BED HYDROPYROLYSIS OF COAL [J].
BOLTON, C ;
SNAPE, CE ;
OBRIEN, RJ ;
KANDIYOTI, R .
FUEL, 1987, 66 (10) :1413-1417
[2]   HETEROATOM DISTRIBUTION IN PYROLYSIS PRODUCTS AS A FUNCTION OF HEATING RATE AND PRESSURE [J].
CAI, HY ;
GUELL, AJ ;
DUGWELL, DR ;
KANDIYOTI, R .
FUEL, 1993, 72 (03) :321-327
[3]   Combustion reactivity and morphological change in coal chars: Effect of pyrolysis temperature, heating rate and pressure [J].
Cai, HY ;
Guell, AJ ;
Chatzakis, IN ;
Lim, JY ;
Dugwell, DR ;
Kandiyoti, R .
FUEL, 1996, 75 (01) :15-24
[4]   THE INFLUENCE OF PYROLYSIS CONDITIONS ON THE REACTIVITY OF CHAR IN H2O [J].
CHITSORA, CT ;
MUHLEN, HJ ;
VANHEEK, KH ;
JUNTGEN, H .
FUEL PROCESSING TECHNOLOGY, 1987, 15 :17-29
[5]  
DAWES SG, 1991, S SERIES I CHEM ENG, V123
[6]   PYROLYSIS AND HYDROPYROLYSIS OF COAL - COMPARISON OF PRODUCT DISTRIBUTIONS FROM A WIRE-MESH AND A HOT-ROD REACTOR [J].
GIBBINS, JR ;
GONENC, ZS ;
KANDIYOTI, R .
FUEL, 1991, 70 (05) :621-626
[7]   VARIABLE-HEATING-RATE WIRE-MESH PYROLYSIS APPARATUS [J].
GIBBINS, JR ;
KING, RAV ;
WOOD, RJ ;
KANDIYOTI, R .
REVIEW OF SCIENTIFIC INSTRUMENTS, 1989, 60 (06) :1129-1139
[8]   COAL PYROLYSIS YIELDS FROM FAST AND SLOW HEATING IN A WIRE-MESH APPARATUS WITH A GAS SWEEP [J].
GIBBINSMATHAM, J ;
KANDIYOTI, R .
ENERGY & FUELS, 1988, 2 (04) :505-511
[9]   DEVELOPMENT OF A GAS-SWEEP FACILITY FOR THE DIRECT CAPTURE OF PYROLYSIS TARS IN A VARIABLE HEATING RATE HIGH-PRESSURE WIRE-MESH REACTOR [J].
GUELL, AJ ;
KANDIYOTI, R .
ENERGY & FUELS, 1993, 7 (06) :943-952
[10]  
GUELL AJ, 1993, FUEL PROCESSING TECH, V8, P8