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Collect. Czech. Chem. Commun. 1990, 55, 2169-2181
https://doi.org/10.1135/cccc19902169

Distribution of solid particles in a mixed vessel

Petr Bílek and František Rieger

Department of Chemical and Food Process Equipment Design, Czech Technical University, 166 07 Prague 6

Crossref Cited-by Linking

  • Fajner D., Pinelli D., Ghadge R.S., Montante G., Paglianti A., Magelli F.: Solids distribution and rising velocity of buoyant solid particles in a vessel stirred with multiple impellers. Chemical Engineering Science 2008, 63, 5876. <https://doi.org/10.1016/j.ces.2008.08.033>
  • Montante G., Bourne J. R., Magelli F.: Scale-Up of Solids Distribution in Slurry, Stirred Vessels Based on Turbulence Intermittency. Ind. Eng. Chem. Res. 2008, 47, 3438. <https://doi.org/10.1021/ie070339v>
  • Montante Giuseppina, Magelli Franco: Mixed Solids Distribution in Stirred Vessels:  Experiments and Computational Fluid Dynamics Simulations. Ind. Eng. Chem. Res. 2007, 46, 2885. <https://doi.org/10.1021/ie060616i>
  • Angst R., Kraume M.: Experimental investigations of stirred solid/liquid systems in three different scales: Particle distribution and power consumption. Chemical Engineering Science 2006, 61, 2864. <https://doi.org/10.1016/j.ces.2005.11.046>
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  • Pinelli D., Montante G., Magelli F.: Dispersion coefficients and settling velocities of solids in slurry vessels stirred with different types of multiple impellers. Chemical Engineering Science 2004, 59, 3081. <https://doi.org/10.1016/j.ces.2004.04.033>
  • Montante Giuseppina, Pinelli Davide, Magelli Franco: Scale-up criteria for the solids distribution in slurry reactors stirred with multiple impellers. Chemical Engineering Science 2003, 58, 5363. <https://doi.org/10.1016/j.ces.2003.09.021>
  • Montante Giuseppina, Pinelli Davide, Magelli Franco: Diagnosis of Solid Distribution in Vessels Stirred with Multiple PBTs and Comparison of Two Modelling Approaches. Can J Chem Eng 2002, 80, 1. <https://doi.org/10.1002/cjce.5450800408>
  • Nocentini M., Pinelli D., Magelli F.: Dispersion coefficient and settling velocity of the solids in agitated slurry reactors stirred with multiple rushton turbines. Chemical Engineering Science 2002, 57, 1877. <https://doi.org/10.1016/S0009-2509(02)00087-8>
  • Pinelli Davide, Magelli Franco: Solids Settling Velocity and Distribution in Slurry Reactors with Dilute Pseudoplastic Suspensions. Ind. Eng. Chem. Res. 2001, 40, 4456. <https://doi.org/10.1021/ie0010518>
  • PINELLI D., NOCENTINI M., MAGELLI F.: SOLIDS DISTRIBUTION IN STIRRED SLURRY REACTORS: INFLUENCE OF SOME MIXER CONFIGURATIONS AND LIMITS TO THE APPLICABILITY OF A SIMPLE MODEL FOR PREDICTIONS. Chemical Engineering Communications 2001, 188, 91. <https://doi.org/10.1080/00986440108912898>
  • Montante G., Micale G., Magelli F., Brucato A.: Experiments and CFD Predictions of Solid Particle Distribution in a Vessel Agitated with Four Pitched Blade Turbines. Chemical Engineering Research and Design 2001, 79, 1005. <https://doi.org/10.1205/02638760152721253>
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  • Magelli F., Nocentini M., Orlandini F., Fajner D., Pinelli D.: Solids Separation at the Exit of a Continuous-Flow Slurry Reactor Stirred with Multiple Axial Impellers. Chemical Engineering Research and Design 1997, 75, 284. <https://doi.org/10.1205/026387697523732>
  • Bohlin Martin, Rasmuson Åke C.: Importance of macromixing in batch cooling crystallization. AIChE Journal 1996, 42, 691. <https://doi.org/10.1002/aic.690420310>