Enhanced mass transfer from the installation of a sieve tray subject to the variation of liquid heights and flow regimes in a bubble column-Reference-Cited by-同舟云学术

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Enhanced mass transfer from the installation of a sieve tray subject to the variation of liquid heights and flow regimes in a bubble column

Published:2018-08 Issue: Volume:136 Page:654-662
ISSN:0263-8762
Container-title:Chemical Engineering Research and Design
language:en
Short-container-title:Chemical Engineering Research and Design

Author:

Im Hanjin,Lee Shinbeom,Lee Jae W.

Funder

Hanwha Chemical R&D Institute

Ministry of Science and ICT, South Korea

Publisher

Elsevier BV

Subject

General Chemical Engineering,General Chemistry

Reference32 articles.

1. Gas holdup and volumetric mass transfer coefficient in bubble columns;Akita;Ind. Eng. Chem. Process Des. Dev.,1973

2. Bubble size, interfacial area, and liquid-phase mass transfer coefficient in bubble columns;Akita;Ind. Eng. Chem. Process Des. Dev.,1974

3. Gas hold-up in bubble columns for Fischer–Tropsch synthesis;Bukur;Chem. Eng. Sci.,1987

4. Measurement of gas holdups and sauter mean bubble diameters in bubble column reactors by dynamics gas disengagement method;Daly;Chem. Eng. Sci.,1992

5. Hydrodynamic properties of the Fischer–Tropsch slurry process;Deckwer;Ind. Eng. Chem. Process Des. Dev.,1980

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