Mass Transfer of Oxygen and Power Consumption with Highly Viscous Liquid in Gas-Liquid Agitated Vessel
PDF

Keywords

Mixing
aeration
oxygen absorption
large paddle impeller

How to Cite

1.
Haruki Furukawa, Kento Matsumoto, Yoshihito Kato, Masataka Kamiya, Masahiro Haitsuka, Noboru Kamei. Mass Transfer of Oxygen and Power Consumption with Highly Viscous Liquid in Gas-Liquid Agitated Vessel. J. Chem. Eng. Res. Updates. [Internet]. 2017 Aug. 31 [cited 2024 Dec. 23];4(1):1-6. Available from: https://avantipublisher.com/index.php/jceru/article/view/887

Abstract

The gas-liquid mass transfer volumetric coefficient (KLa) and power consumption under aeration are important parameters for designing gas-liquid agitated vessel. In this work, KLawas calculated by measuring the dissolved oxygen concentration and the mixing power consumption was calculated by measuringshaft torque in the aerated mixing vessel equipped with several types of large paddle impeller. It was found that the aerated mixing power consumption with the large paddle impellers did not decrease largely, because the large cavity was not formed behind the impeller blade. Then, KLa of large paddle impellers used was correlated with a modified equation of Sato et al. The intercept of Sato’s equation was correlated with the viscosity of CMC aqueous solution. KLaof large paddle impellers is estimated by using the modified Sato’s equation over a wide range of viscosity.

https://doi.org/10.15377/2409-983X.2017.04.01.1
PDF

References

Oyama, Y, Endoh K. Power Characteristics of Gas-Liquid Contacting Mixer. Kagaku Kogaku 1955; 19: 2-8. http://doi.org/10.1252/kakoronbunshu1953.19.2

Calderbank PH. Physical Rate Processes in Industrial Fermentation Part I: The Interfacial Area in Gas-Liquid Contacting with Mechanical Agitation. Trans IChemE 1958; 36: 443-463.

Yatomi R, Takenaka K, Takahashi K, Tanguy PA. Mass Transfer Characteristics by Surface Aeration of Large Paddle Impeller: Application to a Polymerization Reactor with Liquid Level Change. J Chem Eng Japan 2009; 40: 393-397. http://doi.org/10.1252/jcej.40.393

Dohi N, Takahashi T, Minekawa K, Kawase Y. Gas-liquid mass transfer characteristics of large-scale impellers: Empirical correlations of gas holdups and volumetric mass transfer coefficients in stirred tanks. Chem Eng Comm 2006; 193: 689-701. http://dx.doi.org/10.1080/00986440500265885

Takahashi K, Tanimoto I, Sekine H, Takahata Y. Gas Dispersion in Agitated Vessel Equipped with Large Impeller. J Chem Eng Japan 2014; 47: 717-722. http://doi.org/10.1252/jcej.13we338

Takahashi K, Ashino C, Takahata Y. Effect of Gas Dispersion on Mixing Time of Liquid in an Agitated Vessel under Laminar Flow Condition. J Chem Eng Japan 2015; 48: 403- 406. http://doi.org/10.1252/jcej.14we042

Haitsuka M, Kamei N, Kato Y, Kamiya M, Furukawa H, Nagumo R. Power Consumption and Mass Transfer of High Viscosity Liquid in Gas-Liquid Mixing Vessel with Large Paddle Impeller. Kagaku Kougaku Ronbunshu 2016; 42: 174-178. http://doi.org/10.1252/kakoronbunshu.42.174

Aida M, Shono A. Estimation of Power Consumption in Gas- Liquid Stirred Vessels with Various Types of Impellers. Kagaku Kogaku Ronbunshu 2014; 40: 366-371. http://doi.org/10.1252/kakoronbunshu.40.366

Kamei N, Kato Y, Tada Y, Ando J, Nagatsu Y. Effects of Sparger Geometry on Power Consumption and Mass Transfer in a Gas-Liquid Agitated Vessel with Disk Turbine. J Chem Eng Japan 2009; 42: 664-668. http://doi.org/10.1252/jcej.09we110

Sato K, Shimada H, Yoshino Z. Gas Absorption Efficiency of Gas-Liquid Contactors with Mechanical Agitation. Kagaku Kogaku Ronbunshu 1989; 15: 733-739. http://doi.org/10.1252/kakoronbunshu.15.733

Hiraoka S, Tada Y, Kato Y, Ukai Y, Sasaki J, Yamaguchi T, Matsuura A. Power Consumption and Gas-Liquid Mass Transfer Volumetric Coefficient in an Agitated Vessel with Pitched Wire-Gauze Blade Impeller under Aeration. J Chem Eng Japan 2003; 36: 333-338. http://doi.org/10.1252/jcej.36.333

Nishikawa M, Nakamura M, Hashimoto K. Gas Absorption in Aerated Mixing Vessels with Non-Newtonian Liquid. J Chem Eng Japan 1981; 14: 227-232. http://doi.org/10.1252/jcej.14.227

Hiraoka S, Kato Y, Tada Y, Kai S, Inoue N, Ukai Y. Power Consumption and Gas-Liquid Mass Transfer Volumetric Coefficient in a Mechanically Agitated Vessel with Wire- Gauze Impeller. J Chem Eng Japan 2001; 34: 600-605. http://doi.org/10.1252/jcej.34.600

Kato Y. Calculation method and experimental method for the design and operation of mixing equipment. Tokyo: Johokiko 2015; pp.184–185.

Metzner AB, Otto RE. Agitation of Non-Newtonian Fluids. AIChE J 1957; 3: 3-10. http://doi.org/10.1002/aic.690030103

Kuriyama M, Tokanai H, Harada E. Volumetric Mass Transfer Coefficient and Power Consumption in Aerated Agitated Vessels with Higly Viscous Liquids. Kagaku Kougaku Ronbunshu 2002; 28: 188-195.

Creative Commons License

This work is licensed under a Creative Commons Attribution-NonCommercial 4.0 International License.

Copyright (c) 2017 Haruki Furukawa, Kento Matsumoto, Yoshihito Kato, Masataka Kamiya, Masahiro Haitsuka, Noboru Kamei