Abstract
In applications of chemical engineering often the sedimentation is used to separate disperse particles from liquid phases. Some real liquids, e.g., polymer fluids, paints, and skin creams show viscoplastic flow behavior, i.e., they have a yield stress. In such fluids it is possible that suspended particles do not move under action of gravity although the density of the particles is greater than the fluid density. A possibility to sediment stuck spherical particles is shown. The fluid is set in sinusoidal vibration so that the particles undergo forced oscillations. This effect is investigated for single spheres. A model is given and several theoretical results are discussed. A criterion is presented that allows one to predict the combinations of the vibration parameters (amplitude and frequency) which are needed to sediment the spheres. The theoretical investigations are confirmed by experiments. The motion of several glass and steel spheres in an oscillating tube filled with aqueous carbopol solutions are detected. The comparison between theory and experiment shows good agreement.
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Abbreviations
- C :
-
Stokes drag coefficient
- D :
-
strain rate tensor
- E :
-
unit tensor
- F, F w :
-
external resp. drag force
- f :
-
body force vector
- G :
-
Green deformation tensor
- G :
-
dimensionless (shear) modulus
- g :
-
acceleration of gravity
- K :
-
abbreviation (Eq. (15))
- p :
-
pressure
- R, ϑ:
-
spherical coordinates
- R 0, R a :
-
sphere resp. body radius
- T :
-
extra stress tensor
- t :
-
time
- S :
-
stress tensor
- U 0, W 0 :
-
displacement amplitude
- u :
-
displacement vector
- ν:
-
velocity vector
- V :
-
viscoelastic number
- V k :
-
sphere volume
- V ∞ :
-
steady sink velocity
- Y :
-
yield stress parameter
- Y g :
-
limiting value
- Z:
-
Stokes number
- Λ:
-
density ratio
- ή:
-
second invariant of D
- δ:
-
radii ratio
- y:
-
differential viscosity
- λ, μ:
-
Lamé constants
- μ* =μ′ + iμ″:
-
complex (shear) modulus
- ϱf, ϱ k :
-
fluid resp. sphere density
- τ:
-
second invariant of T
- τ f :
-
yield stress
- ϕ:
-
phase angle
- Ω:
-
frequency
References
Ansley RW, Smith TN (1967) Motion of spherical particles in a Bingham plastic. AIChE Journal 13:1193–1196
Beris AN, Tsamopoulos JA, Armstron RC, Brown RA (1985) Creeping motion of a sphere through a Bingham plastic. J Fluid Mech 158:219–244
Bingham EC (1922) Fluidity and plasticity. McGraw Hill, New York
Hunter SC (1968) The motion of a rigid sphere embedded in an adhering elastic and viscoelastic medium. Proc Eding Math Soc 16:55–69
Leonov AI (1988) Extremum principles and exact two bounds of potential: functional and dissipation for slow motions of nonlinear viscoplastic media. J Non-Newt Fluid Mech 28:1–28
Sellers HS, Schwarz WH, Sato M, Pollard T (1987) Boundary effects on the drag of an oscillating sphere: applications to the magnetic sphere rheometer. J Non-Newt Fluid Mech 26:43–55
Stenger M (1989) Ein Ausdruck für die Wechselwirkungskraft zwischen viskoelastischer Flüssigkeit und einer nach harmonischem Zeitgesetz bewegten Kugel. Z angew Math Mech 69:T664-T666
Stokes GG (1851) On the effect of the internal friction on the motion of pendulum. Trans Camb Philos Soc 9(II):8–106
Valentik L, Withmore RL (1965) The terminal velocity of spheres in Bingham plastics. Brit J Appl Phys 16:1197–1203
Wünsch O (1990) Experimentelle Bestimmung Binghamscher Stoffparameter. Rheol Acta 29:163–169
Yoshioka N, Yoshioka N, Adachi K, Ishimura H (1971) On creeping flow of a viscoplastic fluid past a sphere. Kagaku Kogatu 10:1144–1152
Zogg M (1987) Einführung in die mechanische Verfahrenstechnik. B. G. Teubner, Stuttgart
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Wünsch, O. Oscillating sedimentation of spheres in viscoplastic fluids. Rheola Acta 33, 292–302 (1994). https://doi.org/10.1007/BF00366955
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DOI: https://doi.org/10.1007/BF00366955