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Biomass gasification in a bubbling fluidized bed reactor: Experiments and modeling

Radmanesh, Ramin, Chaouki, Jamal, Guy, Christophe·2006·AIChE Journal

Abstract

A model is presented for the gasification of beech wood particles in a bubbling fluidized bed gasifier (BFBG). The model encompasses the hydrodynamics of the solid and gas phases as well as the different reaction kinetics. It also accounts for the freeboard where additional homogeneous reactions take place. The influential impact of the pyrolysis step on the final composition of produced fuel gas was demonstrated by applying two different kinetic models for pyrolysis. Model results are compared with the experimental work of this study and other published results on wood gasification in BFBG. Effects of equivalence ratio (ER), steam to biomass ratio (SB), bed temperature, feed location, and mass transfer between the countercurrent regions (K w) on the gas composition of product fuel gas are studied. The model shows good agreement with the experimental results. © 2006 American Institute of Chemical Engineers AIChE J, 2006

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Metadata

Authors
Radmanesh, R., Chaouki, J., & Guy, C.
Venue
AIChE Journal
Publisher
Wiley
Published
2006-10-10
Volume
52
Issue
12
Pages
4258-4272
ISSN
  • 0001-1541 (ISSN-L)
  • 1547-5905
OpenAlex
W2152510574
Cited by
187
References
0
FWCI
3.17
Type
journal article
Language
en
Open access
closed

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CoChat. (2026). Citation check: Biomass gasification in a bubbling fluidized bed reactor: Experiments and modeling. https://app.cochat.ai/papers/10.1002/aic.11020
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Radmanesh, R., Chaouki, J., & Guy, C. (2006). Biomass gasification in a bubbling fluidized bed reactor: Experiments and modeling. AIChE Journal. https://doi.org/10.1002/aic.11020

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