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SHAPE AND RISING VELOCITY OF BUBBLES
36th Conference of Slovak Society of Chemical Engineering May , Tatranské Matliare SHAPE AND RISING VELOCITY OF BUBBLES Kamil Wichterle, Kateřina Smutná, Marek Večeř VSB-Technical University of Ostrava Faculty of Metallurgy and Material Engineering Department of Chemistry, 70833 Ostrava Poruba, CR Phone: , Fax: ,
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Everyting is known about bubbles
Clift, R., Grace, J.R. and Weber, M.E., 1978: Bubbles, Drops, and Particles. Academic Press, New York. ?
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Classes of bubbles Small bubbles in high-viscosity liquids
Small bubbles in low-viscosity liquids Medium bubbles in high-viscosity liquids Medium bubbles in pure low-viscosity liquids Medium bubbles in contamined low-viscosity liquids Large bubbles
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SIZE OF RISING BUBBLES increasing volume
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LIQUID VISCOSITY Low– and medium-viscosity …. Re > 50
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PURE OR CONTAMINED LIQUID
Pure liquid (surface-active components carefully removed) Mobil surface Lower drag resistance Higher rising velocity Contamined liquid Immobile surface Drag like for solid bodies Lower rising velocity NO QUANTITATIVE PARAMETER !!!
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Focus of our interest Small bubbles
Medium bubbles in pure low-viscosity liquids Medium bubbles in contamined low-viscosity liquids Large bubbles EASY EXPERIMENTS, SIMPLE THEORY Stokes (or Hadamard-Rybczinski) -law COMPLICATED EXPERIMENTS ELLIPSOIDAL BUBBLES, THE MOST COMMON IN BUBBLE COLUMNS PULSATING BUBBLE SHAPE AND VELOCITY, FREQUENT BREAKUP
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LOWER DRAG (hypothetical)
Why not ??
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BUBBLE SHAPE Surface tension Hydrostatics
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SYMMETRIC OBLATE BUBBLE
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Our laboratories
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DETERMINATION OF THE SHAPE OF BUBBLES
Bubble levitating in dowstream flow
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IDEAL OBLATE ELLIPSOID semiaxes a, b
Image analysis Standard procedure how to approximate the bubble: Determination of the projected bubble area Determination of perimeter (usually overestimated)
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IDEAL OBLATE ELLIPSOID semiaxes a, b
Improved procedure: Determination of the object width, height and inclination In front view In side view
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Untreated data
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Reynolds number ?
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Weber number ?
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Eötvös number
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Static bubble profile (under a wetted plate)
„Laplace length!“
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Normalized semiaxes of rising bubbles Theoretical prediction for static bubbles
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RISING VELOCITY
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Time = 10 s , (corresponding path 2,3 m)
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RISING VELOCITY for medium contaminated bubbles
Effects of Viscosity Surface tension Electrolyte
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Our data compared with that of Clift
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Our data compared with that of Tomiyama
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RISING VELOCITY dimensional analysis
Bubble equivalent diameter Gravity acceleration Liquid density Density difference Liquid viscosity Surface tension
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RISING VELOCITY effect of surface tension
Morton number Dimensionless bubble diameter Dimensionless bubble velocity „Laplace velocity“ Viscosity cannot be neglected !!
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RISING VELOCITY classical variables
Drag coefficient Not very successful !!
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RISING VELOCITY effect of viscosity
Drag coefficient Dimensionless bubble diameter Dimensionless bubble velocity There is still an effect of surface tension!!
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RISING BUBBLE Oscillatory movement of a bubble Bubble front area is S = p a2 New definition of the drag coefficient
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New dimensionless variables
OK !!!
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RESULTING FORMULAS Correlation of the bubble shape
Correlation of the bubble velocity This correlation fits well the data for medium size bubbles in contaminated low- and medium- viscosity liquids. In carefully prepared pure liquids, the rising velocity of can be somewhat higher.
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Thank you for your attention
Acknowledgments We gratefully acknowledge financial support by the grant No.104/07/1110 from the Grant Agency of the Czech Republic.
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