There is substantial disagreement over the order of the reaction between a coal char and O2. This is chiefly because of the difficulties of making good measurements when burning is kinetically controlled; thus heat and mass transfer can often obscure the true kinetics of the reaction. Consequently, a fluidized bed is an attractive reactor in which to measure the rate of this reaction. Chars from three different coals (of high, medium and low ranks) were prepared. The rate of oxidation of a char was measured by adding a small mass (∼ 3 mg) of tiny particles (sieved to 106–150 μm) of the char to a fluidized bed of silica sand (90–126 μm), which was electrically heated to a fixed temperature between 700 and 950°C. The fluidizing gas was a mixture of O2 and N2 at 1 bar; its composition varied between 0 and 100% O2. The concentrations of CO and CO2 were continuously measured in the off-gases from the bed, using i.r. analysers, thus enabling the rate of oxidation of the added batch of char to be measured. Interestingly, it was found necessary to modify the quartz cylinder housing the fluidized bed to prevent backmixing of ambient air into the freeboard. The char particles were sufficiently small that mass transfer to their exteriors did not control the rate of reaction. Furthermore, the rapid rates of heat transfer from the bed to the particles of char ensured that the char burned at the temperature of the bed. Likewise, the mass of added char was small enough for the rate of burning not to be controlled by inter-phase mass transfer. The maximum rate of oxidation was taken to be the initial rate, which could, at least in principle, be correlated with the initial properties of a char, such as its BET area, pore diameters, etc. The char of the low-rank coal burned with kinetics which were zeroth order in O2 and with a negligible activation energy. The other two coals had orders of reaction which were 0.7–0.8 at 700°C, but 0.2–0.25 at 950°C. These orders are discussed in detail.
Skip Nav Destination
18th International Conference on Fluidized Bed Combustion
May 22–25, 2005
Toronto, Ontario, Canada
Conference Sponsors:
- Advanced Energy Systems
ISBN:
0-7918-4183-9
PROCEEDINGS PAPER
The Kinetics of Oxidation of Chars From Three Different Coals, as Measured in Fluidized Beds
P. S. Fennell,
P. S. Fennell
University of Cambridge, Cambridge, UK
Search for other works by this author on:
A. N. Hayhurst,
A. N. Hayhurst
University of Cambridge, Cambridge, UK
Search for other works by this author on:
J. S. Dennis,
J. S. Dennis
University of Cambridge, Cambridge, UK
Search for other works by this author on:
S. Kadchha,
S. Kadchha
University of Cambridge, Cambridge, UK
Search for other works by this author on:
H.-Y. Lee
H.-Y. Lee
University of Cambridge, Cambridge, UK
Search for other works by this author on:
P. S. Fennell
University of Cambridge, Cambridge, UK
A. N. Hayhurst
University of Cambridge, Cambridge, UK
J. S. Dennis
University of Cambridge, Cambridge, UK
S. Kadchha
University of Cambridge, Cambridge, UK
H.-Y. Lee
University of Cambridge, Cambridge, UK
Paper No:
FBC2005-78073, pp. 881-894; 14 pages
Published Online:
October 7, 2008
Citation
Fennell, PS, Hayhurst, AN, Dennis, JS, Kadchha, S, & Lee, H. "The Kinetics of Oxidation of Chars From Three Different Coals, as Measured in Fluidized Beds." Proceedings of the 18th International Conference on Fluidized Bed Combustion. 18th International Conference on Fluidized Bed Combustion. Toronto, Ontario, Canada. May 22–25, 2005. pp. 881-894. ASME. https://doi.org/10.1115/FBC2005-78073
Download citation file:
8
Views
Related Proceedings Papers
Related Articles
Hydrodynamic Performance of a Novel Design of Pressurized Fluidized Bed Combustor
J. Energy Resour. Technol (June,2006)
Operating Experience With a Fluidized Bed Test Combustor
J. Energy Resour. Technol (June,1987)
Nonradiative Heat Transfer Coefficients and “Cold” Operating Experience With a Laboratory SCFBC Model
J. Energy Resour. Technol (June,1986)
Related Chapters
Gas-Fluidized Beds
Two-Phase Heat Transfer
Calculated Tolerance of a Large Electric Utility Gas Turbine to Erosion Damage by Coal Gas Ash Particles
Erosion: Prevention and Useful Applications
A Microstructural Modeling-Based Approach to Graphite Oxidation beyond ASTM D7542
Graphite Testing for Nuclear Applications: The Validity and Extension of Test Methods for Material Exposed to Operating Reactor Environments