WOLFRAM|DEMONSTRATIONS PROJECT

Bingham Fluid Flow in a Circular Tube

​
yield stress
0.15
zero-shear viscosity
0.05
A Bingham fluid acts like a rigid body at low shear stress but flows like a viscous fluid at high shear.
Consider the laminar flow of a Bingham fluid in a long circular tube of radius
R=0.01m
and length
L=1m
. The fluid flows under the influence of a pressure difference
ΔP=100N/
2
m
. The fluid density is
ρ=0.75kg/l
.
One can derive an analytical expression for the velocity, given by http://www.syvum.com/cgi/online/serve.cgi/eng/fluid/fluid807.html:
v
z
=
ΔP
2
R
4
μ
0
L
1-
2
r
R
-
τ
0
R
μ
0
1-
r
R
for
R⩾r⩾
r
0
,
v
z
=
ΔP
2
R
4
μ
0
L
1-
2
r
0
R
for
r⩽
r
0
,
where
r
0
=
2L
τ
0
ΔP
.
The mass flow rate is given by:
w=
R
∫
0
2πρr
v
z
dr=
ΔP
4
R
ρπ
8
μ
0
L
1-
4
τ
0
3
τ
R
+
1
3
4
τ
0
τ
R
, with
τ
R
=
ΔPR
2L
.
Here
μ
0
is the zero–shear viscosity and
τ
0
is the yield stress. You can vary these two parameters.
For a Newtonian fluid, the mass flow rate is given by the Hagen–Poiseuille equation:
w=
ΔP
4
R
ρπ
8μL
.
This Demonstration plots the velocity profile (blue curve) and gives the value of the corresponding mass flow rate. In addition, the velocity profile for a Newtonian fluid is plotted (red curve). The viscosity,
μ
, of the Newtonian fluid is chosen such that both fluid mass flow rates are equal. The value of the viscosity,
μ
, is also shown.