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An experimental study of double‐to‐single‐loop transition in stirred vessels
Author(s) -
Montante G.,
Brucato A.,
Lee K. C.,
Yianneskis M.
Publication year - 1999
Publication title -
the canadian journal of chemical engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.404
H-Index - 67
eISSN - 1939-019X
pISSN - 0008-4034
DOI - 10.1002/cjce.5450770405
Subject(s) - impeller , turbulence , rushton turbine , mixing (physics) , mechanics , flow (mathematics) , axial compressor , loop (graph theory) , materials science , slip factor , rotational speed , physics , thermodynamics , mathematics , classical mechanics , quantum mechanics , combinatorics , gas compressor
The velocity characteristics of the flows in a fully baffled vessel of diameter T = 290 mm stirred by a Rushton impeller of diameter D = T/3 were investigated by means of laser‐Doppler anemometry measurements. The effects of clearance and rotational speed on the flow patterns in the vessel were studied. It was found that at impeller clearances from the bottom of the vessel ( C ) around 0.2 T the characteristic double‐loop flow pattern undergoes a transition to a single‐loop one with the impeller stream direction becoming partly axial and being inclined at around 25 to 30° to the horizontal. The impeller stream inclination varied with radial distance from the impeller, as well as with angular position between blades (blade angle). Impeller speed was found to have no effect on the flow pattern or the mean velocities and turbulence levels normalized by V tip for C/T > 0.20 or C/T ≤ 0.15. The flow structure measured with C = 0.15 T is described in detail and the implications of the data for fluid mixing in stirred vessels are discussed.