CFD simulation of two- and three-phase flow in FCC reactors
Liquid distribution and evaporation in Fluid Catalytic Cracking (FCC) reactors are investigated numerically. The well-documented inaccuracy of conventional two-fluid modeling of hydrodynamics in fluidized beds of Geldart Group A particles is revisited. A new force-balance (FB) sub-grid-scale model,...
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| Language: | English |
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University of British Columbia
2015
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| Online Access: | http://hdl.handle.net/2429/52621 |