LrgpV1, Main, Exploration, bibRecord, 000E68

Biomass Fast Pyrolysis: Experimental Analysis and Modeling Approach : Bioenergy and Green Engineering

Identifieur interne : 000E68 ( Main/Exploration ); précédent : 000E67; suivant : 000E69

Biomass Fast Pyrolysis: Experimental Analysis and Modeling Approach : Bioenergy and Green Engineering

Auteurs : M. Al-Haddad [France] ; E. Rendek [France] ; J.-P. Corriou [France] ; G. Mauviel [France]

Source :

Energy & fuels [ 0887-0624 ] ; 2010.

RBID : Pascal:10-0497769

Descripteurs français

Pascal (Inist)
- Biomasse, Pyrolyse, Modélisation, Bilan masse, Cinétique, Phase solide, Transfert chaleur, Modèle 2 dimensions, Méthode volume fini, Four, Flux thermique, Densité, Etude comparative.
Wicri :
- topic : Biomasse, Four.

English descriptors

KwdEn :
- Biomass, Comparative study, Density, Finite volume method, Furnace, Heat flow, Heat transfer, Kinetics, Mass balance, Modeling, Pyrolysis, Solid phase, Two dimensional model.
mix :
- BEHAVIOR, CELLULOSE PELLETS, DEVOLATILIZATION, FLUIDIZED-BED REACTOR, KINETICS, PARTICLE, RADIANT FLASH PYROLYSIS, TRANSIENT, WOOD PYROLYSIS.

Abstract

A single particle model able to predict the evolution of the product yields during biomass fast pyrolysis is developed. Mass balance equations based on a kinetic scheme of solid-phase pyrolysis are coupled to heat-transfer equations. This two-dimensional model is solved by the finite volume method. The model results are compared to experimental data obtained in an image furnace, where biomass pellets are submitted to a controlled and concentrated radiation. Heat flux densities that are available at the biomass surface are similar to those encountered in fluidized beds (0.2-0.8 x 10⁶ W m^-2). The comparison between the experimental data and simulated results shows that the kinetic parameters need to be further optimized to accurately represent the final product yields.

Url:

https://hal.archives-ouvertes.fr/hal-00798960

Affiliations:

Le document en format XML

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<front><div type="abstract" xml:lang="en">A single particle model able to predict the evolution of the product yields during biomass fast pyrolysis is developed. Mass balance equations based on a kinetic scheme of solid-phase pyrolysis are coupled to heat-transfer equations. This two-dimensional model is solved by the finite volume method. The model results are compared to experimental data obtained in an image furnace, where biomass pellets are submitted to a controlled and concentrated radiation. Heat flux densities that are available at the biomass surface are similar to those encountered in fluidized beds (0.2-0.8 x 10<sup>6</sup>
 W m<sup>-2</sup>
). The comparison between the experimental data and simulated results shows that the kinetic parameters need to be further optimized to accurately represent the final product yields.</div>
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Biomass Fast Pyrolysis: Experimental Analysis and Modeling Approach : Bioenergy and Green Engineering

Biomass Fast Pyrolysis: Experimental Analysis and Modeling Approach : Bioenergy and Green Engineering

Source :

Descripteurs français

English descriptors

Abstract

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