Gas-Liquid Mass Transfer Coefficient of a Pitched Bladed Paddle Up-Pumping at Extraordinary Large Gas Flow Rates
Author:
Affiliation:
1. Process Development Research Laboratories, Lion Corp.
2. Department of Materials Science and Energy Engineering, Yamagata University
3. Department of Chemistry and Chemical Engineering, Yamagata University
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
http://www.jstage.jst.go.jp/article/jcej/39/8/39_8_783/_pdf
Reference17 articles.
1. Calderbank, P. H.; “Physical Rate Processes in Industrial Fementation. Part 1: The Interfacial Area in Gas–Liquid Contacting with Mechanical Agitation,” Trans. Inst. Chem. Eng., 36, 443–463 (1958)
2. Gas-liquid mixing studies with multiple up- and down-pumping hydrofoil impellers: Power characteristics and mixing time
3. Hickman, A. D.; “Gas–Liquid Oxygen Transfer and Scale-up. A Novel Agitated Vessels,” Proc. of the 6th European Conf. on Mixing, pp. 369–374, BHRA, Cranfield, Pavia, Italy (1988)
4. A critical review and experimental verification of the correct use of the dynamic method for the determination of oxygen transfer in aerated agitated vessels to water, electrolyte solutions and viscous liquids
5. Nienow, A. W.; “Gas–Liquid Mixing Studies: A Comparison of Rushton Turbine with Some Modern Impellers,” Trans. Inst. Chem. Eng., 74, 417–423 (1996)
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1. Effect of Gas Dispersion on Mixing Time of Liquid in an Agitated Vessel under Laminar Flow Condition;Journal of Chemical Engineering of Japan;2015
2. Scale up and Effect of Sparger Position on Power Consumption and Mass Transfer in Mixing Vessel with Disk Turbine;KAGAKU KOGAKU RONBUNSHU;2012
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