Solid-catalyzed reaction in a fluidized bed

Results are presented for the solid‐catalyzed hydrogenation of ethylene in fixed and fluidized beds. The effect of gas velocity, bed height, catalyst activity, particle size, and internal baffles on fluidized reactor efficiency are given, and Equations derived from a simplified mathematical model co...

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Veröffentlicht in:AIChE journal 1959-12, Vol.5 (4), p.419-426
Hauptverfasser: Lewis, W. K., Gilliland, E. R., Glass, Werner
Format: Artikel
Sprache:eng
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Zusammenfassung:Results are presented for the solid‐catalyzed hydrogenation of ethylene in fixed and fluidized beds. The effect of gas velocity, bed height, catalyst activity, particle size, and internal baffles on fluidized reactor efficiency are given, and Equations derived from a simplified mathematical model correlate the data.
ISSN:0001-1541
1547-5905
DOI:10.1002/aic.690050405