Startseite Liquid Flow and Mixing in Bottom Regions of Baffled and Unbaffled Vessels Agitated by Turbine-Type Impeller
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Liquid Flow and Mixing in Bottom Regions of Baffled and Unbaffled Vessels Agitated by Turbine-Type Impeller

  • Masanori Yoshida EMAIL logo , Naoki Shimada , Rei Kanno , Satoshi Matsuura und Yohei Otake
Veröffentlicht/Copyright: 30. Oktober 2014
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Abstract

For a vessel agitated by the turbine-type impeller, the liquid flow and mixing in the bottom region were studied for comparison between conditions with and without baffles. Visualization of the flow and its measurement were done using particle tracking velocimetry. The flow along the bottom surface of the unbaffled vessel was observed to be more intensified than that of the baffled one. The related local energy dissipation was larger and the effective energy transmission was indicated for the condition without the baffles. For the unbaffled vessel, enhancement of micromixing near the bottom was demonstrated through a mixing experiment in a system involving chemical reactions.

Nomenclature

Di

impeller diameter, mm

Dt

vessel diameter, mm

R

radial distance, mm

Rt

vessel radius, mm

vr

radial velocity component of liquid flow, m/s

vz

axial velocity component of liquid flow, m/s

vθ

circumferential velocity component of liquid flow, m/s

Xs

segregation index, -

Y

observed yield of undesired product, -

Yst

stoichiometric yield of undesired product, -

Z

axial distance, mm

α

micromixedness ratio, -

ε

local energy dissipation rate per unit mass of liquid, W/kg

εL

locally averaged energy dissipation rate per unit mass of liquid, W/kg

εt

totally averaged energy dissipation rate per unit mass of liquid, W/kg

μ

viscosity of liquid, mPa · s

Θ

circumferential angle, °

ρ

density of liquid, kg/m3

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Published Online: 2014-10-30
Published in Print: 2014-1-1

©2014 by De Gruyter

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