Journal
PROCEEDINGS OF THE COMBUSTION INSTITUTE
Volume 34, Issue -, Pages 2373-2381Publisher
ELSEVIER SCIENCE INC
DOI: 10.1016/j.proci.2012.06.054
Keywords
Fast pyrolysis; Discrete element method; Biomass; Fluidised bed
Funding
- EPSRC [EP/I000801/1]
- Engineering and Physical Sciences Research Council [EP/I000801/1] Funding Source: researchfish
- EPSRC [EP/I000801/1] Funding Source: UKRI
Ask authors/readers for more resources
A 3D Eulerian/Lagrangian simulation incorporating multi-step reaction mechanisms has been used to study fast pyrolysis of biomass in a 100 g/h fluidised bed reactor. The overall goal to optimise the production of bio-oil from fast pyrolysis is largely dependent on the thermochemical degradation process inside fluidised bed reactors. The discrete representation of biomass and sand particles in the simulation bridges accurate numerical modelling with reproducing realistic phenomena seen experimentally. Herein, the hydrodynamic bed behaviour causes temperature variations among batches of biomass particles injected at different times. It is found that such disparity affects the instantaneous tar release, causing relatively large differences in tar quantity and quality. (C) 2012 The Combustion Institute. Published by Elsevier Inc. All rights reserved.
Authors
I am an author on this paper
Click your name to claim this paper and add it to your profile.
Reviews
Recommended
No Data Available