## Abstract A reactor model is presented to calculate the sulfur retention and SO~2~ emission of a fluidizedโbed coal combustor with absorption of SO~2~ by limestone or dolomite. It is based on the twoโphase theory of fluidization and a two parameter simplified rate expression for the sulfation rea
A technique for determining devolatilization rates of large coal particles in a fluidized bed combustor
โ Scribed by Tabarik F. Salam; Xian Ling Shen; Bernard M. Gibbs
- Publisher
- Elsevier Science
- Year
- 1988
- Tongue
- English
- Weight
- 663 KB
- Volume
- 67
- Category
- Article
- ISSN
- 0016-2361
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โฆ Synopsis
A non-interference technique has been developed for measuring devolatilization rates of large coal particles in a cylindrical fluidized bed at 850ยฐC by on-line analysis of oxygen and carbon dioxide concentrations in the flue gas. The experiments were conducted over a range of inlet oxygen concentrations (3-10 ~01%). Oxygen concentrations were analysed by a xirconia probe, and carbon dioxide concentrations were analysed by an on-line infrared gas analyser. Associated problems and suitability of the measuring technique are discussed. A bituminous coal (d= 9-16.3mm) was used and devolatilization periods > 130s were observed. The devolatilization times showed a dependence on the inlet oxygen concentration, particularly at the lower (3 ~01%) inlet oxygen concentration.
A simple calculation to demonstrate the need for considering devolatilization rates. 'coal' disnersion coetlicients. excess air levels and combustor geometry in FBC I modelling is also given.
๐ SIMILAR VOLUMES
Coal particles with diameters of 3-11 mm were injected into a small, hot bed of sand fluidized by nitrogen. Volatiles evolution was followed by sampling the exit gas stream and subsequent analysis by gas chromatography. Three Australian coals covering a range of volatile matter were studied and the