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Analysis of volume change effects in a fluidized bed catalytic reactor
Author(s) -
Shiau ChingYeh,
Lin ChinJou
Publication year - 1993
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.280560313
Subject(s) - bubble , volume fraction , volume (thermodynamics) , fluidized bed , emulsion , thermodynamics , fraction (chemistry) , mechanics , materials science , phase (matter) , chemistry , chromatography , physics , organic chemistry
A mathematical model based on the concept of an improved bubble assemblage model is developed for calculating the conversion of a reaction system involving a volume change in fluidized beds. The influence of volume change on the hydrodynamic behavior of gas in the bed, such as bubble size variation, superficial gas velocity change, and volume fraction occupied by each phase, is also investigated. It is found that increasing stoichiometric coefficient values results in larger bubble size, higher superficial gas velocities, higher crossflow rate between emulsion phase and bubble phase, and greater volume fraction of bubble phase, but smaller volume fraction occupied by the emulsion phase as well as lower conversions.