The virtual mass coefficient is determined experimentally for the motion of two spheres side by side and in line in a power law fluid. The velocities of the two accelerating spheres and their separation distance was measured as they accelerated under the action of driving weights through a cylindrical column filled with different concentrations of polyacryamaide solution (0.01%, 0.03%, 0.05%, and 0.07% by weight). For comparison purposes, the experiments were repeated with water. Various densities of spheres and separation distances were examined. Within the range of power law indices (0.61–0.834) and Reynolds numbers (1.1–75) examined, the virtual mass coefficient was found to decrease with an increasing Reynolds number for the two spheres moving side by side, and found to be greater than 0.5 when the spheres were touching each other. As the distance between the spheres increased, the virtual mass coefficient was found to decrease and approached the single sphere value of 0.5 when the distance between the spheres was more than ten radii. When the spheres were in line and touching each other, the virtual mass coefficient was found to be less than 0.5, however, when the distance between the spheres increased, the virtual mass coefficient increased and approached the value of 0.5. The virtual mass coefficient was found to be consistent with the shear thinning behavior; for a given Reynolds number, it increased with an increasing power law index.

1.
Huber
,
A.
, 2006, “
Pollution Dispersion in Urban Landscapes
,” FLUENT News, Internet, pp.
11
16
.
2.
Clift
,
R.
,
Grace
,
J. R.
, and
Weber
,
M. E.
, 1978,
Bubbles, Drops and Particles
,
Academic
,
New York
.
3.
Bagchi
,
A.
, and
Chhabra
,
R. P.
, 1991, “
Acceleration Motion of Spherical Particles in Power Law Type Non-Newtonian Liquids
,”
Powder Technol.
0032-5910,
68
, pp.
85
90
.
4.
Chhabra
,
R. P.
,
Soares
,
A.
, and
Ferreira
,
J. M.
, 1998, “
A Numerical Study of the Accelerating Motion of a Dense Rigid Sphere in Non-Newtonian Power Law Fluids
,”
Can. J. Chem. Eng.
0008-4034,
76
, pp.
1051
1055
.
5.
Zhu
,
C.
,
Lam
,
K.
,
Tang
,
X.
, and
Liu
,
G.
, 2003, “
Drag Forces of Interacting Spheres in Power-Law Fluids
,”
Mech. Res. Commun.
0093-6413,
30
, pp.
651
662
.
6.
Michaelides
,
E. E.
, 2003, “
Hydrodynamic Force and Heat/Mass Transfer From Particles, Bubbles, and Drops—The Freeman Scholar Lecture
,”
ASME J. Fluids Eng.
0098-2202,
125
, pp.
209
238
.
7.
Odar
,
F.
, and
Hamilton
,
W. S.
, 1964, “
Forces on a Sphere Accelerating in a Viscous Fluid
,”
J. Fluid Mech.
0022-1120,
18
, pp.
302
314
.
8.
Kelessidis
,
V.
, 2003, “
Terminal Velocity of Solid Spheres Falling in Newtonian and Non-Newtonian Liquids
,”
Techn. Chron. Sci. J., Techn. Chamber Greece
,
V
(
1–2
), pp.
43
54
.
9.
Kelessidis
,
V.
, 2004, “
Measurements and Prediction of Terminal Velocity of Solid Spheres Falling Through Stagnant Pseudoplastic Liquids
,”
Powder Technol.
0032-5910,
147
, pp.
117
125
.
10.
Leichtberg
,
S.
,
Weinbaum
,
S.
,
Pfeffer
,
R.
, and
Gluckman
,
M. J.
, 1976, “
A Study of Unsteady Forces at Low Reynolds Numbers: A Strong Interaction Theory for the Coaxial Settling of Three or More Spheres
,”
Philos. Trans. R. Soc. London
0962-8428,
282
, pp.
585
610
.
11.
Legendre
,
D.
,
Magnaudet
,
J.
, and
Mougin
,
G.
, 2003, “
Hydrodynamic Interactions Between Two Spherical Bubbles Rising Side by Side in a Viscous Liquid
,”
J. Fluid Mech.
0022-1120,
497
, pp.
133
166
.
12.
Tsuji
,
Y.
,
Morikawa
,
Y.
, and
Terashima
,
K.
, 1982, “
Fluid-Dynamic Interaction Between Two Spheres
,”
Int. J. Multiphase Flow
0301-9322,
8
, pp.
71
82
.
13.
Zhu
,
C.
,
Liang
,
S. C.
, and
Fan
,
L. S.
, 1994, “
Particle Wake Effect on the Drag Force of an Interactive Particle
,”
Int. J. Multiphase Flow
0301-9322,
20
, pp.
117
129
.
14.
Helfinstine
,
R. A.
, and
Dalton
,
C.
, 1974, “
Unsteady Potential Flow Past a Group of Spheres
,”
Comput. Fluids
0045-7930,
2
, pp.
99
112
.
15.
Kendoush
,
A. A.
,
Sulaymon
,
A. H.
, and
Mohammed
,
S. A.
, 2007, “
Experimental Evaluation of Virtual Mass of Two Spheres in Fluids
,”
Exp. Therm. Fluid Sci.
0894-1777,
31
, pp.
813
823
.
16.
Cai
,
X.
, and
Wallis
,
G. B.
, 1994, “
A More General Cell Model for Added Mass in Two-Phase Flow
,”
Chem. Eng. Sci.
0009-2509,
49
(
10
), pp.
1631
1638
.
17.
Ruzicka
,
M. C.
, 2000, “
On Bubbles Rising in Line
,”
Int. J. Multiphase Flow
0301-9322,
26
, pp.
1141
1181
.
18.
Kumagai
,
T.
, and
Muraoka
,
M.
, 1989, “
On Motion of Spheres in a Fluid at Low Reynolds Numbers
,”
JSME Int. J.
0913-185X,
32
, pp.
309
316
.
19.
Alwared
,
A. I.
, 2008, “
Hydrodynamic of Spheres in Various Solutions
,” Ph.D. thesis, Baghdad University, Iraq.
20.
Abbad
,
M.
, and
Souhar
,
M.
, 2004, “
Effect of the History Force on an Oscillating Rigid Sphere at Low Reynolds Number
,”
Exp. Fluids
0723-4864,
36
, pp.
775
782
.
21.
Kim
,
I.
,
Elghobashi
,
S.
, and
Sirignano
,
W. A.
, 1998, “
On the Equation for Spherical Particle Motion: Effect of Reynolds and Acceleration Numbers
,”
J. Fluid Mech.
0022-1120,
367
, pp.
221
253
.
22.
Miura
,
H.
,
Takahashi
,
T.
,
Ichikawa
,
J.
, and
Kawase
,
Y.
, 2001, “
Bed Expansion in Liquid–Solid Two-Phase Fluidized Beds With Newtonian and Non-Newtonian Fluids Over the Wide Range of Reynolds Numbers
,”
Powder Technol.
0032-5910,
117
, pp.
239
246
.
23.
Pinelli
,
D.
, and
Magelli
,
F.
, 2001, “
Solids Falling Velocity and Distribution in Slurry Reactors With Dilute Pseudoplastic Suspensions
,”
Ind. Eng. Chem. Res.
0888-5885,
40
, pp.
4456
4462
.
24.
Ford
,
J. T.
, and
Oyeneyin
,
M. B.
, 1994, “
The Formulation of Milling Fluids for Efficient Hole Cleaning: An Experimental Investigation
,”
European Petroleum Conference
, London, UK, SPE Paper No. 28819, pp.
25
27
.
25.
Haider
,
A.
, and
Levenspiel
,
O.
, 1989, “
Drag Coefficient and Terminal Velocity of Spherical and Nonspherical Particles
,”
Powder Technol.
0032-5910,
58
, pp.
63
70
.
26.
Alexander
,
P.
, 2004, “
High Order Computation of the History Term in the Equation of Motion for a Spherical Particle in a Fluid
,”
J. Sci. Comput.
0885-7474,
21
(
2
), pp.
129
143
.
27.
Lawrence
,
C. J.
, and
Mei
,
R. W.
, 1995, “
Long-Time Behavior of the Drag on a Body in an Impulsive Motion
,”
J. Fluid Mech.
0022-1120,
283
, pp.
307
327
.
28.
Mordant
,
N.
, and
Pinton
,
J. F.
, 2000, “
Velocity Measurement of a Settling Sphere
,”
Eur. J. Phys.
0143-0807,
B18
, pp.
343
352
.
29.
Hollander
,
W.
, and
Zairpov
,
S. K.
, 2005, “
Hydrodynamically Interacting Droplets at Small Reynolds Numbers
,”
Int. J. Multiphase Flow
0301-9322,
31
, pp.
53
68
.
30.
Daily
,
J. W.
, and
Harleman
,
D. R. F.
, 1966,
Fluid Dynamics
,
Addison-Wesley
,
Canada
.
31.
Darwin
,
C.
, 1953, “
A Note on Hydrodynamics
,”
Proc. Cambridge Philos. Soc.
0068-6735,
49
, pp.
342
354
.
32.
Magnaudet
,
J.
, and
Eames
,
I.
, 2000, “
The Motion of High Reynolds Number Bubbles in Inhomogeneous Flows
,”
Annu. Rev. Fluid Mech.
0066-4189,
32
, pp.
659
708
.
33.
Moorman
,
R. B.
, 1955, “
Motion of a Spherical Particle in the Accelerated Portion of a Free Fall
,” Ph.D. thesis, State University of Iowa, Iowa.
34.
Takahashi
,
K.
, and
Endoh
,
K.
, 1992, “
A Virtual Mass and Drag Coefficient for an Oscillating Particle
,”
J. Chem. Eng. Jpn.
0021-9592,
25
(
6
), pp.
683
685
.
35.
Holman
,
J. P.
, 1984,
Experimental Methods for Engineers
,
McGraw-Hill
,
New York
.
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