Intraparticle mass transfer in coal pyrolysis
- 1 March 1980
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 26 (2) , 201-212
- https://doi.org/10.1002/aic.690260203
Abstract
Intraparticle mass transfer in coal pyrolysis is described by ternary diffusion and viscous flow, in conjunction with a simple pore model to predict concentration profiles for gases and tar. At low pressures, product yields depend on particle size only, while at high pressures they depend on pressure and particle size. Limited experimental data from a subbituminous coal confirm these trends. Data from a bituminous coal show different trends, as expected from the drastic changes the pore structure undergoes during pyrolysis.This publication has 15 references indexed in Scilit:
- A model for short residence time hydropyrolysis of single coal particlesAIChE Journal, 1979
- Characterization of the heavy products of coal pyrolysisFuel, 1978
- An analytical study of single particle char gasificationAIChE Journal, 1978
- Product Composition and Kinetics of Lignite PyrolysisIndustrial & Engineering Chemistry Process Design and Development, 1978
- Rapid devolatilization and hydrogasification of bituminous coalFuel, 1976
- Reaction with mole changes in porous catalysts in the molecular, transition, and Knudsen regimesAIChE Journal, 1973
- Graham's laws: Simple demonstrations of gases in motion: Part I, TheoryJournal of Chemical Education, 1969
- Application of the single pellet reactor for direct mass transfer studies II. Measurement of composition at center of catalyst pelletJournal of Catalysis, 1968
- Significance of pressure gradients in porous materials: Part III. Effect of pressure gradients on the effectiveness of porous catalystsAIChE Journal, 1965
- Diffusion and reaction in porous glassAIChE Journal, 1964