Pressure drop, holdup and interfacial area in vertical two-phase flow of multi-jet ejector induced dispersions-Reference-Cited by-同舟云学术

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Pressure drop, holdup and interfacial area in vertical two-phase flow of multi-jet ejector induced dispersions

Published:1984-04 Issue:2 Volume:62 Page:170-178
ISSN:0008-4034
Container-title:The Canadian Journal of Chemical Engineering
language:en
Short-container-title:Can. J. Chem. Eng.

Author:

Radhakrishnan V. R.,Mitra A. K.

Publisher

Wiley

Subject

General Chemical Engineering

Reference32 articles.

1. “Effective Interfacial Area in a Liquid-jet Induced Horizontal Gas-Liquid Pipeline Contactor”;Biswas;Indian Chem. Eng,1977

2. “The Design of Gas Absorbers”;Danckwerts;Trans. Inst. Chem. Engrs,1966

3. “Oxygen Transfer and Circulation Rate in Activated Sudge Channels”;Daucher;Ger. Chem. Eng,1982

4. “The Effect of the Froude number in estimating vertical 2-phase gas-liquid friction losses”;Davis;Brit. Chem. Eng,1963

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3. Numerical Simulation of Bubble Coalescence and Break-Up in Multinozzle Jet Ejector;Journal of Applied Mathematics;2016

4. Databases of interfacial area concentration in gas–liquid two-phase flow;Progress in Nuclear Energy;2014-07

5. Gas holdup and energy dissipation in liquid-gas ejectors;Journal of Chemical Technology & Biotechnology;2008

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