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Studies of mixing time and momentum transfer for an agitated with an off-centred impeller

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
In many industrial processes, the final technological effect related to the product quality strictly depends on the efficiency of agitation. The effects of the impeller eccentricity and liquid pumping mode of the impeller on the liquid homogenisation and momentum transfer processes are discussed in the paper. The mixing time tm in an un - baffled agitated vessel of working volume V = 0.27 m^3 was measured using thermal method. The dimensionless shear rate gamma/n and friction coefficient f on the cylindrical wall of the vessel of the volume V = 0.022 m^3 were determined by means of an electrochemical method. The distribution of both gamma/n and f values is found as a function of the impeller eccentricity eR for a propeller and HE 3 impeller. The data for dimensionless mixing time were correlated using Eq. (1). The values of gamma/n and f, averaged for the whole cylindrical wall, were described for both the propeller and HE 3 impeller, by means of Eqs. (2) - (5).
Rocznik
Strony
35--42
Opis fizyczny
Bibliogr. 23 poz., tab., rys.
Twórcy
autor
autor
autor
  • Szczecin University of Technology, Institute of Chemical Engineering and Environmental Protection Processes, al. Piastów 42, 71-065 Szczecin, joanka@ps.pl
Bibliografia
  • (1) Ruszkowski S. W.: A rational method for measuring blending performance and comparison of different impeller types. IChemE Symposium Series, 1994, 136, 283 - 291.
  • (2) Ashrafi N., Binding D. M., Walters K.: Cavitation effects in eccentric - cylinder flows of Newtonian and non-Newtonian fluids. Chem. Eng. Sci., 2001, 56, 5565 - 5574.
  • (3) Papadias D., Edsberg L., Bjornbom P.: Effect of eccentricity and interaction between kinetics and mass transfer on the behaviour of catalytic annular reactors: a comparison between lumped and distributed models. Chem. Eng. Sci., 2001, 56, 4863 - 4878.
  • (4) Dyląg M., Brauer H.: Leistungsbedarf bei exzentrischer Anordnung des Ruehres. Verfahrenstechnik, 1976, 10, 10, 637 - 640.
  • (5) Karcz J., Cudak M., Szoplik J.: Stirring of a liquid in a stirred tank with an eccentrically located impeller. Chem. Eng. Sci., 2005, 60, 8-9, 2369 - 2380.
  • (6) Karcz J., Cudak M.: Efficiency of the heat transfer process in a jacketed agitated vessel equipped with an eccentrically located impeller. Chem. Pap., 2002, 56(6), 382 - 386.
  • (7) King R., Muskett J.: Fluid loading and power measurements on an eccentrically mounted pitched blade impeller. Proceed., Paper 29, pp. 285 - 301, 5th European Conf. on Mixing, Wuerzburg, Germany, 10 - 12.06.1985.
  • (8) Stręk F.: Mieszanie i mieszalniki. Wyd. II, WNT, Warszawa, 1981.
  • (9) Tatterson G. B.: Fluid Mixing and Gas Dispersion in Agitated Tanks. McGraw-Hill, Inc., New York, 1991.
  • (10) Karcz J., Cudak M., Kiełbus A.: Power consumption for axial flow impeller located eccentrically in a stirred tank. Paper P221, 9 pp, Proceed. of the 30th Intern. Conf. of Society of Chem. Eng. (on CD-ROM), Tatranske Matliare, Slovakia, 26 - 30.05.2003.
  • (11) Karcz J., Szoplik J.: An effect of the eccentric position of the propeller agitator on the mixing time. Chem. Pap., 2004, 58, 1, 9 - 14.
  • (12) Szoplik J., Karcz J.: An efficiency of the liquid homogenization in agitated vessels equipped with off – centred impeller. Chem. Pap., 2005, 59, 6a, 373 - 379.
  • (13) Szoplik J.: The studies of the mixing time in a stirred tank with an eccentrically located impeller. PhD Thesis, Szczecin University of Technology, 2004.
  • (14) Seichter P., Pesl L., Slama V., Mazoch J.: Blending effect of excentric axial agitators. Paper E3.2, 14th Intern. Congress of Chem. and Proc. Eng. CHISA, Praha, Czech Republic, 27 - 31. 08. 2000.
  • (15) Ascanio G., Brito - Bazan M., Brito - De La Fuente E., Carreau P. J., Tanguy P. A.: Unconventional configuration studies to improve mixing time in stirred tanks. Canadian J. of Chem. Eng., 2002, 80, 4, 558 - 565.
  • (16) Cudak M.: Heat and momentum transfer in a stirred tank with an eccentrically located impeller. PhD Thesis, Szczecin University of Technology, 2004.
  • (17) Montante G., Bakker A., Paglianti A., Magelli F: Effect of the shaft eccentricity on the hydrodynamics of unbaffled stirred tanks. Chem. Eng. Sci., 2006, 61, 2807 - 2814.
  • (18) Shaw J. A.: Understand the effects of impeller type, diameter, and power on mixing time. Chem. Eng. Prog., 1994, 9, 2, 45 - 48.
  • (19) Karcz J., Cudak M.: Local momentum and heat transfer in a liquid and gas - solid - liquid systems mechanically stirred in a jacketed vessel. Proceed., ed. by VDI - GVC, pp. 447 - 454, 11th European Conf. on Mixing, Bamberg, Germany, 14 - 17.09.2003.
  • (20) Karcz J.: Momentum transfer in a region of an agitated vessel wall. Inż Chem. Proc., 1996, 17, 3, 403 - 421.
  • (21) Stręk F., Karcz J.: Zastosowanie metody elektrochemicznej do badania transportu masy w obszarze przyściennym mieszalnika cieczy. Inż. Chem. Proc., 1999, 20, 3 - 22.
  • (22) Wichterle K., Mitschka P., Hajek J., Zak L.,: Shear stresses on the walls of vessels with axial impellers. Chem. Eng. Res. Des., 1988, 66, 102 - 106.
  • (23) Wichterle K., Zak L., Mitschka P.: Shear stresses on the walls of agitated vessel. Chem. Eng. Commun., 1985, 32, 289 – 305
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPS2-0037-0019
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