Modelling of non-catalytic gasβsolid rea
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B.S. Sampath; P.A. Ramachandran; R. Hughes
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Article
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1975
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Elsevier Science
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English
β 732 KB
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