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
✦ LIBER ✦
Modelling and simulation of the flux responses of a gas–solid catalytic micro-reactor
✍ Scribed by B.A Buffham; K Hellgardt; M.J Heslop; G Mason; D.J Richardson
- Book ID
- 108311001
- Publisher
- Elsevier Science
- Year
- 2002
- Tongue
- English
- Weight
- 209 KB
- Volume
- 57
- Category
- Article
- ISSN
- 0009-2509
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