A gas-solid reaction model for flash wood pyrolysis
โ Scribed by M.A. Hastaoglu; F. Berruti
- Publisher
- Elsevier Science
- Year
- 1989
- Tongue
- English
- Weight
- 882 KB
- Volume
- 68
- Category
- Article
- ISSN
- 0016-2361
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โฆ Synopsis
A theoretical modelling study of wood flash pyrolysis has been carried out using the single pellet technique. The model considers the transient behaviour of a single wood particle undergoing a fast thermal decomposition reaction. Mass transfer, pressure gradients in the pellet, heat transfer via convection, conduction and radiation, and structural changes occurring in the particle are accounted for. The wood particle is assumed to consist of libres of hollow cylindrical shape. The pyrolysis reaction occurs at an interface within each fibre, which moves with time. The kinetic mechanism for the reaction assumes the wood to decompose according to two parallel reactions yielding tar and and (gas +char). Tar is then assumed to decompose further by secondary homogeneous cracking reactions to yield gas. The results of the modelling work compare favourably with experimental data of conversion and temperature over a wide range of operating temperatures.
๐ SIMILAR VOLUMES
A mathematical model of the pyrolysis of wet particles of wood is presented. The model integrates: (i) a conventional description of the physical and chemical phenomena involved in the pyrolysis pf dry particles of wood, and (ii) a simplified drying model. The dry-pyrolysis model assumes a complex r
## Abstract Analysis of singleโpore behavior in a porous pellet of reactant is used to develop a new model for predicting the conversionโtime relationship for gasโsolid noncatalytic reactions. The model accounts for the influence of pore diffusion, diffusion through the product layer which builds u
A parallel plate model is suggested for describing noncatalytic gas-solid reactions. Based on this model, expressions are developed which relate explicitly the progress of the reaction to porosity of the solid matrix, diffisivities in the pore and in the ash, reactant concentrations in the gas phase