Coal combustion characteristics in a circulating fast fluidized bed |
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Authors: | Geun Seong Lee Gui Young Han Sang Done Kim |
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Affiliation: | (1) Department of Chemical Engineering, Korea Advanced Institute of Science and Technology, P.O.Box 131, 131 Dongdaemun, Seoul, Korea |
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Abstract: | The effect of coal size (0.73–1.03 mm), excess air ratio (1.0–1.4), operating bed temperature (750–900‡C), coal feeding rate
(1–3 kg/h), and coal recycle rate (20–40 kg/h) on combustion efficiency, temperature profiles along the bed height and flue
gas composition have been determined in a bubbling and circulating fluidized bed combustor (7.8 cm-ID x 2.6 m-high).
Combustion efficiency increases with increasing excess air ratio and operating bed temperature and it decreases with increasing
particle size in the bubbling and circulating fluidzing beds. In general, temperature profiles and combustion efficiency are
more uniform and higher in a circulating bed than those in bubbling bed. Combustion efficiency also increases with increasing
recycle rate of unburned coal in the circulating bed.
The ratio of CO/CO2 of flue gas decreases with increasing bed temperature and excess air ratio, whereas the ratio of O2(CO + CO2) decreases with bed temperature in both bubbling and circulating fluidized beds. |
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