| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 6644060 | Fuel | 2012 | 13 Pages |
Abstract
⺠We validated a CFD model for biomass fast pyrolysis in a lab-scale fluidized bed. ⺠Simulations achieve good quantitative agreement with experimental data. ⺠Particle size and gas velocity influence tar yield and residence time considerably. ⺠Reactor temperature is critical for product yields. ⺠The model is able to differentiate between feedstocks in terms of product yields.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Q. Xue, D. Dalluge, T.J. Heindel, R.O. Fox, R.C. Brown,