A non-interference technique has been developed for measuring devolatilization rates of large coal particles in a cylindrical fluidized bed at 850°C by on-line analysis of oxygen and carbon dioxide concentrations in the flue gas. The experiments were conducted over a range of inlet oxygen concentrat
Devolatilization of wood particles in a hot fluidized bed: Product yields and conversion rates
✍ Scribed by S. Rapagnà; G. Mazziotti di Celso
- Publisher
- Elsevier Science
- Year
- 2008
- Tongue
- English
- Weight
- 626 KB
- Volume
- 32
- Category
- Article
- ISSN
- 0961-9534
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✦ Synopsis
Spherical wood particles of various well-defined diameters were fed into a bed of fluidized olivine maintained at temperatures in the range of 700-900 1C. The fluidizing gas was either nitrogen or a steam-nitrogen mixture, and the wooden spheres were introduced in two different ways: on to the bed surface and deep into the bed itself. The resulting gas, tar and char yields were found to be influenced by the method of feed introduction as well as by the bed temperature, fluidizing gas composition and wood particle diameter. The total devolatilization time was correlated by means of a power law expression similar to that used for coal devolatilization and having the advantage of being able to fit well the experimental data over the full temperature range in both nitrogen and steam-nitrogen atmospheres.
📜 SIMILAR VOLUMES
An experimental study on the segregation of fuel particles and of volatile matter during devolatilization in a fluidized-bed reactor is presented. The study was purposely carried out with beds of solids kept at incipient fluidization in order to focus attention on the segregation phenomena associate
the flue gas led from the lower side is contacted with the finely small drops for desulfurization and dust removal. The contact efficiency of the flue gas and the absorbent liquid is increased, resulting in efficient desulfurization.