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18th International Conference on Fluidized Bed Combustion | 2005

The Kinetics of Oxidation of Chars From Three Different Coals, as Measured in Fluidized Beds

P.S. Fennell; A.N. Hayhurst; John S. Dennis; S. Kadchha; H.-Y. Lee

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.Copyright


Chemical Engineering Science | 2006

The nature of the flow just above the perforated plate distributor of a gas-fluidised bed, as imaged using magnetic resonance

A.C. Rees; J.F. Davidson; John S. Dennis; P.S. Fennell; Lynn F. Gladden; A.N. Hayhurst; M.D. Mantle; Christoph R. Müller; Andrew J. Sederman


Physical Review Letters | 2006

Real-time measurement of bubbling phenomena in a three-dimensional gas-fluidized bed using ultrafast magnetic resonance imaging.

Christoph R. Müller; J.F. Davidson; John S. Dennis; P.S. Fennell; Lynn F. Gladden; A.N. Hayhurst; M.D. Mantle; A.C. Rees; Andrew J. Sederman


Chemical Engineering Science | 2007

The measurement of the rate of burning of different coal chars in an electrically heated fluidised bed of sand

P.S. Fennell; S. Kadchha; H.-Y. Lee; John S. Dennis; A.N. Hayhurst


Proceedings of the Combustion Institute | 2005

The rate of gasification by CO2 of chars from waste

Stuart A. Scott; J.F. Davidson; John S. Dennis; P.S. Fennell; A.N. Hayhurst


Chemical Engineering Science | 2005

A study of the mixing of solids in gas-fluidized beds, using ultra-fast MRI

P.S. Fennell; J.F. Davidson; John S. Dennis; Lynn F. Gladden; A.N. Hayhurst; M.D. Mantle; Christoph R. Müller; A.C. Rees; Stuart A. Scott; Andrew J. Sederman


Powder Technology | 2007

Oscillations in gas-fluidized beds: Ultra-fast magnetic resonance imaging and pressure sensor measurements

Christoph R. Müller; J.F. Davidson; John S. Dennis; P.S. Fennell; Lynn F. Gladden; A.N. Hayhurst; M.D. Mantle; A.C. Rees; Andrew J. Sederman


Chemical Engineering Science | 2007

Rise velocities of bubbles and slugs in gas-fluidised beds: Ultra-fast magnetic resonance imaging

Christoph R. Müller; J.F. Davidson; John S. Dennis; P.S. Fennell; Lynn F. Gladden; A.N. Hayhurst; M.D. Mantle; A.C. Rees; Andrew J. Sederman


Proceedings of the Combustion Institute | 2009

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

P.S. Fennell; John S. Dennis; A.N. Hayhurst


Combustion and Flame | 2011

Combustion of polymer pellets in a bubbling fluidised bed

F. Burgess; P.D.W. Lloyd; P.S. Fennell; A.N. Hayhurst

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A.C. Rees

University of Cambridge

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M.D. Mantle

University of Cambridge

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H.-Y. Lee

University of Cambridge

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S. Kadchha

University of Cambridge

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