| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 10397458 | Chemical Engineering and Processing: Process Intensification | 2005 | 20 Pages |
Abstract
In a second step a model of the CFB gasifier was developed. The fluid dynamics of a CFB were included as well as the complete reaction network of gasification. With the measured axial profiles of gas composition during pyrolysis, and gasification with air and a CO2/N2-mixture kinetic rate expressions for sewage sludge gasification under fluidized-bed conditions were determined which may now be used for reactor scale-up calculations.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Process Chemistry and Technology
Authors
I. Petersen, J. Werther,