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Biomass Gasification with Steam in Fluidized Bed: Effectiveness of CaO, MgO, and CaO−MgO for Hot Raw Gas Cleaning

Delgado, Jesús, Aznar, María P., Corella, José·1997·Industrial & Engineering Chemistry Research

Abstract

The upgrading of the raw hot gas from a bubbling fluidized bed biomass gasifier is studied using cheap calcined minerals or rocks downstream from the gasifier. Biomass gasification is made with steam (not air) at 750−780 °C and about 0.5−1.0 kg of biomass/h. Calcined solids used are dolomite (MgO−CaO), pure calcite (CaO), and pure magnesite (MgO). Variables studied have been temperature of the secondary bed (780−910 °C), time of contact or space-time of the gas (0.08−0.32 kg·h/m 3 n), and particle diameter (1−4 mm) and type of mineral. Their effects on tar conversion, tar amount in the exit gas, product distribution, and gas composition are presented. Using a macrokinetic model for the tar disappearance network, the activities of the stones are expressed by their apparent kinetic constant. Apparent energies of activation for tar elimination (42−47 kJ/mol) and preexponential and effectiveness factors are given for all tested solids of which the most active is the calcined dolomite.

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Metadata

Authors
Delgado, J., Aznar, M. P., & Corella, J.
Venue
Industrial & Engineering Chemistry Research
Published
1997-05-01
Volume
36
Issue
5
Pages
1535-1543
ISSN
  • 0888-5885 (ISSN-L)
  • 1520-5045
OpenAlex
W2089543826
Cited by
326
References
0
FWCI
6.17
Type
journal article
Language
en
Open access
closed

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CoChat. (2026). Citation check: Biomass Gasification with Steam in Fluidized Bed: Effectiveness of CaO, MgO, and CaO−MgO for Hot Raw Gas Cleaning. https://app.cochat.ai/papers/10.1021/ie960273w
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Delgado, J., Aznar, M. P., & Corella, J. (1997). Biomass Gasification with Steam in Fluidized Bed: Effectiveness of CaO, MgO, and CaO−MgO for Hot Raw Gas Cleaning. Industrial & Engineering Chemistry Research. https://doi.org/10.1021/ie960273w

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