Effect of Sparger Design and Height to Diameter Ratio on Fractional Gas Hold-up in Bubble Columns-Reference-Cited by-同舟云学术

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Effect of Sparger Design and Height to Diameter Ratio on Fractional Gas Hold-up in Bubble Columns

Published:1998-10 Issue:7 Volume:76 Page:823-834
ISSN:0263-8762
Container-title:Chemical Engineering Research and Design
language:en
Short-container-title:Chemical Engineering Research and Design

Author:

Thorat B.N.,Shevade A.V.,Bhilegaonkar K.N.,Aglawe R.H.,Parasu Veera U.,Thakre S.S.,Pandit A.B.,Sawant S.B.,Joshi J.B.

Publisher

Elsevier BV

Subject

General Chemical Engineering,General Chemistry

Reference19 articles.

1. Hold-up liquid circulation in bubble columns;Freedman;Trans IChemE,1969

2. Gas hold-up in uniformly aerated bubble column reactors;Zahradnik;Chem Eng Commun,1979

3. Gas hold-up behavior in a tall bubble column with perforated plate distributors;Tsuchiya;Chem Eng Sci,1992

4. Experimental studies of gas void fraction froth height on a perforated plate-low clear liquid height under liquid stagnant flow;Takahashi;J Chem Eng Japan,1974

5. Mass transfer characteristics of low H/D bubble columns;Gopal;Can J Chem Eng,1983

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