Transient model for packed bed non-catalytic reactors, which avoids many of the simplifying assumptions of the earlier models, has been developed. The model includes the effects of inter-and intra-pellet transfer resistances and the additional effects of axial dispersion in the bulk fluid. The solut
Modelling of non-catalytic gas—solid reactions—I. Transient analysis of the particle—pellet model
✍ Scribed by B.S. Sampath; P.A. Ramachandran; R. Hughes
- Publisher
- Elsevier Science
- Year
- 1975
- Tongue
- English
- Weight
- 845 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0009-2509
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