Bubble sizes in agitated air–alcohol systems with and without particles: Turbulent and transitional flow

Author:

Hu B.,Pacek A.W.,Stitt E.H.,Nienow A.W.

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference15 articles.

1. Mass transfer in gas–liquid slurry reactors;Beenackers;Chemical Engineering Science,1993

2. The dependency on scale of power numbers of Rushton disc turbines;Bujalski;Chemical Engineering Science,1987

3. Some effects of particle wettability in agitated solid-gas-liquid systems: gas–liquid mass transfer and dispersion of floating solids;Gentile;The Canadian Journal of Chemical Engineering,2003

4. Harnby, N., Edwards, M.F., Nienow, A.W. (Eds.), 1997. Mixing in the Process Industries (second edition paperback). Butterworth-Heinemann, Oxford, UK.

5. The effect of sodium caseinate concentration and processing conditions on bubble sizes and their break-up and coalescence in turbulent, batch air/aqueous dispersions at atmospheric and elevated pressures;Hu;Colloids and Surfaces B: Biointerfaces,2003

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