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Destabilisation of a homogeneous bubbly flow in an annular gap bubble column

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journal contribution
posted on 2010-11-24, 17:16 authored by Fahd M. Al-Oufi, Iain W. Cumming, Chris Rielly
Experimental results are presented to show that there are very significant differences in the mean gas void fractions measured in an open tube and a annular gap bubble column, when operated at the same gas superficial velocity, using a porous sparger. The mean gas void fraction decreases with increasing ratio of the inner to outer diameter of the annular gap column and the transition to heterogeneous flow occurs at lower gas superficial velocities and lower void fractions. Two reasons are proposed and validated by experimental investigations: (1) the presence of the inner tube causes large bubbles to form near the sparger, which destabilize the homogeneous bubbly flow and reduce the mean void fraction; this was confirmed by deliberately injecting large bubbles into a homogeneous dispersion of smaller bubbles and (2) the shape of the void fraction profiles changes with gap geometry and this affects the distribution parameter in the drift flux model.

Funding

Void fraction profiles, heterogeneous flow, flow transition, two-point conductivity probe

History

School

  • Aeronautical, Automotive, Chemical and Materials Engineering

Department

  • Chemical Engineering

Citation

AL-OUFI, F.M., CUMMING, I.W. and RIELLY, C.D., 2010. Destabilisation of a homogeneous bubbly flow in an annular gap bubble column. The Canadian Journal of Chemical Engineering, 88 (4), pp.482–490.

Publisher

Wiley (© Canadian Society for Chemical Engineering)

Version

  • AM (Accepted Manuscript)

Publication date

2010

Notes

This is a pre-publication version of an article published in The Canadian Journal of Chemical Engineering.

ISSN

1939-019X

Language

  • en

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