A Combined Numerical and Experimental Study of Hydrodynamics for an Air-Water External Loop Airlift Reactor
Author(s) -
Deify Law,
Samuel T. Jones,
Theodore J. Heindel,
Francine Battaglia
Publication year - 2011
Publication title -
journal of fluids engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.529
H-Index - 103
eISSN - 1528-901X
pISSN - 0098-2202
DOI - 10.1115/1.4003424
Subject(s) - mechanics , computational fluid dynamics , bubble , airlift , work (physics) , multiphase flow , superficial velocity , flow (mathematics) , bubble column reactor , range (aeronautics) , eulerian path , materials science , volumetric flow rate , physics , thermodynamics , gas bubble , chemistry , bioreactor , organic chemistry , composite material , mathematical physics , lagrangian
The external loop airlift reactor (ELALR) is a modified bubble column reactor that is composed of two vertical columns that are interconnected with two horizontal tubes and is often preferred over traditional bubble column reactors because they can operate over a wider range of conditions. In the present work, the gas-liquid flow dynamics in an ELALR was simulated using an Eulerian―Eulerian ensemble-averaging method in two-dimensional (2D) and three-dimensional (3D) coordinate systems. The computational fluid dynamics (CFD) simulations were compared to experimental measurements from a 10.2 cm diameter ELALR for superficial gas velocities ranging from 1 cm/s to 20 cm/s. The effect of specifying a mean bubble diameter to represent the gas phase in the CFD modeling was investigated, and 2D and 3D simulations were found to be in good agreement with the experimental data. The ELALR flow regimes were compared for the reactor operating in bubble column, closed vent, and open vent modes, and the 2D simulations qualitatively predicted the behavior of bubble growth in the downcomer. However, it was found that 3D simulations were necessary to capture the physics of the ELALR for gas holdup, bulk density differences, and riser superficial liquid velocity.
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