Article ID Journal Published Year Pages File Type
155354 Chemical Engineering Science 2013 11 Pages PDF
Abstract

The influence of particle size (dP) and solid concentration (Cs) on the hydrodynamics of a slurry bubble column were studied experimentally using ultrafast electron beam X-ray tomography. Experiments were carried out for dP=50–150 μm at Cs=0–0.20 and superficial gas velocity UG=0.02–0.05 m/s in a slurry bubble column of diameter DT=0.07 m. The real time 3D gas flow structure, average bubble diameter and averaged gas hold-up were found to be independent of dP and Cs at small dP≤100 μm and low Cs≤0.03, however, at large dP and high Cs, strong dependency on dP and Cs were observed. Corresponding three-phase simulations were also performed using the Euler–Euler multi-fluid model implemented in CFX 14. The bubble size distribution was calculated using the MUSIG model. The predicted gas hold-up and bubble size distribution also shows dependence on dP and agreed quite well with the measurements and previous studies.

► Ultrafast electron beam X-ray tomography is used to investigate the hydrodynamics inside a slurry bubble column. ► Bubble size distribution and gas hold-up are measured as a function of particle size. ► Three phase simulation with MUSIG model implemented in CFX 14 is used. ► Validation of predicted gas hold-up and bubble size with experimental results.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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