The order with respect to oxygen and the activation energy for the burning of an anthracitic char in O2 in a fluidised bed, as measured using a rapid analyser for CO and CO2

被引:37
作者
Fennell, P. S. [1 ]
Dennis, J. S. [1 ]
Hayhurst, A. N. [1 ]
机构
[1] Univ Cambridge, Dept Chem Engn, Cambridge CB2 3RA, England
关键词
Char oxidation; Fluidisation; Order of oxidation; Fast analysers; COMBUSTION; KINETICS; CARBON;
D O I
10.1016/j.proci.2008.06.097
中图分类号
O414.1 [热力学];
学科分类号
070201 [理论物理];
摘要
Measurements of the oxidation of a coal char in a fluidised bed have the advantages that the rates of heat and mass transfer to and from a reacting particle are large and characterised well. However, problems have arisen from a combination of the slow, but typical, response-time (similar to 4 s) of the analysers for CO and CO(2) and the slow mixing of gases when filling a fairly large fluidised bed. The resulting time constant for the sampling system vas similar to 8 s and comparable to the time for combustion at 900 degrees C or above. The purpose of this work was to measure the kinetics of oxidation of a char in a smaller fluidised bed (with a shorter mixing time) using an analyser for CO and CO(2) with a response time as low as 0.1 s. The result is that the oxidation of an anthracitic char is now found to be first order in O(2) between 700 and 900 degrees C; at 900 degrees C the order previously measured was almost zero. The activation energy is now measured here to be 145 +/- 25 kJ/mol, in agreement with some early work. (C) 2009 The Combustion Institute. Published by Elsevier Inc. All rights reserved.
引用
收藏
页码:2051 / 2058
页数:8
相关论文
共 12 条
[1]
The order, arrhenius parameters, and mechanism of the reaction between gaseous oxygen and solid carbon [J].
Bews, IM ;
Hayhurst, AN ;
Richardson, SM ;
Taylor, SG .
COMBUSTION AND FLAME, 2001, 124 (1-2) :231-245
[2]
Bird R B., 2002, Transportphenomena
[3]
The kinetics of combustion of chars derived from sewage sludge [J].
Dennis, JS ;
Lambert, RJ ;
Milne, AJ ;
Scott, SA ;
Hayhurst, AN .
FUEL, 2005, 84 (2-3) :117-126
[4]
Variation of the pore structure of coal chars during gasification [J].
Feng, B ;
Bhatia, SK .
CARBON, 2003, 41 (03) :507-523
[5]
The measurement of the rate of burning of different coal chars in an electrically heated fluidised bed of sand [J].
Fennell, P. S. ;
Kadchha, S. ;
Lee, H. -Y. ;
Dennis, J. S. ;
Hayhurst, A. N. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :608-618
[6]
FENNELL PS, 2005, P FBC 18 ONT CAN
[7]
THE COMBUSTION OF CARBON-MONOXIDE IN A 2-ZONE FLUIDIZED-BED [J].
HAYHURST, AN ;
TUCKER, RF .
COMBUSTION AND FLAME, 1990, 79 (02) :175-189
[8]
Semi-global intrinsic kinetics for char combustion modeling [J].
Hurt, RH ;
Calo, JM .
COMBUSTION AND FLAME, 2001, 125 (03) :1138-1149
[9]
Reply to Letter to the Editor by Sun et al. - "The synergistic effect between macerals during pyrolysis"" [J].
Kandiyoti, R .
FUEL, 2002, 81 (07) :975-975
[10]
LONG W, 2006, ENERG FUEL, V20, P2572