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A study on blending characteristics of axial flow impellers

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Języki publikacji
EN
Abstrakty
EN
This paper presents an analysis of the blending characteristics of axial flow high-speed impellers under a turbulent regime of flow of an agitated low viscosity liquid. The conductivity method is used to determine the time course of blending (homogenisation) of miscible liquids in a pilot plant fully baffled mixing vessel, and a torquemeter is used for measuring the impeller power input in the same system. Four-blade and six-blade pitched blade impellers and three high efficiency axial flow impellers are tested for the given degree of homogeneity (98%). The experimental results and also the results of the authors' previous study, in accordance with the theoretical approach described in the literature, show that there is a universal relationship between the impeller power number and the dimensionless blending time, taking into consideration the impeller-to-vessel diameter ratio, independent of the geometry of the axial flow impeller but dependent on the degree of homogeneity. This relationship is found to be valid on a pilot plant scale under a turbulent flow regime of an agitated liquid.
Rocznik
Strony
311--319
Opis fizyczny
Bibliogr. 11 poz., rys., tab.
Twórcy
autor
autor
  • Czech Technical University in Prague, Faculty of Mechanical Engineering, Department of Process Engineering, Technicka 4, 166 07 Prague 6, Czech Republic
Bibliografia
  • 1. Fort I., 1989. Flow and turbulence in vessels with axial impellers, In: Uhl V.W., Gray J.B. (Eds.), Mixing, theory and practice, Vol. III. Academic Press, New York, 133 - 197.
  • 2. Fort I., Jirout T., Rieger F., Allner R., Sperling R., 2001. Study of the blending efficiency of pitched blade impellers. Acta Polytechnica ,41,7- 13.
  • 3. Grenville R. K., Nienow A. W., 2003. Blending in miscible liquid, In: Paul E. L., Otiemo-Obeng V. A., Kresta S. M. (Eds.), Industrial mixing. Science and practice. Wiley Interscience, New York, 507 - 542.
  • 4. Khang S. J., Levenspiel O., 1976. New scale-up and design criteria for stirrer agitated batch mixing vessels. Chem Eng. Sci., 31, 569-577. DOI: 10.1016/0009-2509(76)80020-6.
  • 5. Kramers H., Baars G. M., Knoll W. H., 1953. A comparative study on the rate of mixing in stirred tanks. Chem. Eng. Sci., 2, 35-42. DOI: 10.1016/0009-2509(53)80006-0.
  • 6. Liu M., 2011a. Prediction of tracer concentration and mixing in CFSTR with mean age distribution. Ind. Eng. Chem. Res., 50, 5838 - 5851. DOI: 10.1021/ie2002395.
  • 7. Liu M., 2011b. Quantitative characterisation of mixing in stirred tank reactors with mean age distribution. Can. Jour. Chem. Eng., 89, 1018-1028. DOI: 10.0122/cjce.20563.
  • 8. Mavros P., Xuereb C, Fort I., Bertrand J., 2002. Investigation by laser Doppler velocimetry of the effects of liquid flow rates and feed positions on the flow patterns induced in a stirred tank by an axial - flow impeller. Chem. Eng. Sci., 57, 3939 - 3952. DOI: 10.1016/0009 - 2509(02)00268-3.
  • 9. Nienow A. W., 1997. On impeller circulation and mixing effectiveness in the turbulent regime. Chem. Eng. Sci, 52 , 2557-2565. DOI: 10.1016/0009 - 2509(97)00072-9.
  • 10. Prochazka J., Landau J., 1961. Homogenization of miscible liquids by rotary impellers. Collect. Czech. Chem. Commun., 26, 2961-2974.
  • 11. Seichter P., Pesl L., 2005. Design of rotary impellers - science or art? CHEMagazin, 15(2), 8-11 (in Czech).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPK6-0014-0042
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