Several materials that are of interest in engineering present a yield stress and behave as viscoplastic fluids. This paper investigates numerically the motion of a Bingham fluid between two coaxial cylinders due to a periodic pressure gradient and/or to the periodic displacement of the internal cylinder. The constitutive equation presents a discontinuity at the zero shear rate. To overcome the difficulty, the rheologic law has been regularized using a smooth function based on the error function. The velocity fields have been calculated using an implicit finite difference method. The procedure has been validated, comparing the numerical results with the analytical solution of the same problem for a Newtonian fluid. The nonlinear behavior of the fluid is emphasized, comparing the effects due to the simultaneous action of the pressure gradient and the displacement of the internal wall with the sum of the effects due to the single actions. In all cases, the mean discharge in a period increases. The comparison between the effects of the forcing agents shows that if the dimensionless frequency is less than 10 the increases of the discharge obtained by applying the pulsatile pressure gradient or moving the internal wall are similar. At low frequencies the action of the gradient exceeds that of the moving wall, whereas for higher frequencies the effect of the moving wall increases rapidly because a fixed displacement of the internal cylinder leads to very great values for the velocity of the internal wall.

References

1.
Bird
,
R. B.
,
Dai
,
G. C.
, and
Yarusso
,
B. J.
, 1983, “
The Rheology and Flow of Viscoplastic Materials
,”
Rev. Chem. Eng.
,
1
, pp.
1
67
.
2.
Fredrickson
,
A. G.
, and
Bird
,
R. B.
, 1958, “
Non-Newtonian Flow in Annuli
,”
Ind. Eng. Chem.
50
, pp.
347
352
.
3.
Liu
,
Y. Q.
, and
Zhu
,
K. Q.
, 2010, “
Axial Couette-Poiseuille Flow of Bingham Fluids Through Concentric Annuli
,”
J. Non-Newtonian Fluid Mech.
,
165
, pp.
1494
1504
.
4.
Soares
,
E. J.
,
Naccache
,
M. F.
, and
Mendes
,
P. R. S.
, 2003, “
Heat Transfer to Viscoplastic Materials Flowing Axially Through Concentric Annuli
,”
Int. J. Heat Fluid Flow
,
24
(
5
), pp.
762
773
.
5.
Glowinski
,
R.
, 1984,
Numerical Methods for Non-Linear Variational Problems
,
Springer-Verlag
,
New York
.
6.
Papanastasiou
,
T. C.
, 1987, “
Flows of Materials With Yield
,”
J. Rheol.
,
31
(
5
), pp.
385
404
.
7.
Frigaard
,
I. A.
, and
Nouar
,
C.
, 2005, “
On the Usage of Viscosity Regularization Methods for Visco-Plastic Fluid Flow Computation
,”
J. Non-Newtonian Fluid Mech.
,
127
, pp.
1
26
.
8.
Duggins
,
R. K.
, 1972, “
The Commencement of Flow of a Bingham Plastic Fluid
,”
Chem. Eng. Sci.
,
27
, pp.
1991
1996
.
9.
Papanastasiou
,
T. C.
, and
Boudouvis
,
A. G.
, 1977, “
Flows of Viscoplastic Materials: Models and Computation
,”
Comp. Struct.
,
64
(
1–4
), pp.
677
694
.
10.
Hammad
,
K. J.
, 1998, “
Unsteady Pipe Flows of a Viscoplastic Non-Newtonian Fluid: Effects of Pressure Gradient Waveform
,”
Proc. ASME FED
,
247
, pp.
197
204
.
11.
Barnes
,
H. A.
, 1999, “
The Yield Stress – A Review or ‘παντα ρει’ – Everything Flows?
J. Non-Newtonian Fluid Mech.
,
81
, pp.
133
178
.
12.
Daprà
,
I.
, and
Scarpi
,
G.
, 2010, “
Unsteady Simple Shear Flow in a Viscoplastic Fluid: Comparison Between Analytical and Numerical Solutions
,”
Rheol. Acta
,
49
, pp.
15
22
.
You do not currently have access to this content.