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Measurements and computation of low mass transfer coefficients for FCC particles with ozone decomposition reaction
Author(s) -
Kashyap Mayank,
Gidaspow Dimitri
Publication year - 2012
Publication title -
aiche journal
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.958
H-Index - 167
eISSN - 1547-5905
pISSN - 0001-1541
DOI - 10.1002/aic.12615
Subject(s) - sherwood number , mass transfer , reynolds number , fluidized bed , decomposition , computational fluid dynamics , thermodynamics , chemistry , kinetic energy , ozone , mass transfer coefficient , schmidt number , mechanics , physics , classical mechanics , organic chemistry , turbulence , nusselt number
The mass transfer coefficients and Sherwood numbers for catalyzed fluid cracking catalyst particles were measured and computed in a two‐dimensional (2‐D) bubbling fluidized bed, with ozone decomposition reaction. The measured and computed Sherwood numbers, using 3‐ and 2‐D kinetic theory based computational fluid dynamics simulations, were of the order of 10 −6 –10 −2 . The low Sherwood numbers were in reasonable agreement with the literature data for small particles, at low Reynolds numbers. The computational fluid dynamics simulations showed that it is possible to compute conversions in fluidized bed reactors without using the conventional model with empirical mass transfer coefficients. © 2011 American Institute of Chemical Engineers AIChE J, 2012