Biomedical Engineering Reference
In-Depth Information
Thus, applying the constitutive relation ( 3 )toEq.( 1 ), the Navier-Stokes
equations for incompressible Newtonian fluids are obtained:
ρ
u
t + ρ (
u
· )
u
+
p
div
(
2
μ
D
(
u
)) =
0
,
(4)
in
Ω ,∀
t
>
0
,
div u
=
0
.
3.2
Generalized Newtonian Fluids
The most general form of Eq. ( 2 ), for isotropic symmetric tensor functions, under
frame invariance requirements [ 21 ], is given by
+ φ 2 D 2
σ = φ 0 I
+ φ 1 D
,
(5)
with
φ 0 , φ 1 ,
and
φ 2 dependent on the density
ρ
and on the three principal invariants
2 (
) ,and III D =
1
2
D 2
of D , I D =
tr
(
D
)
, II D =
tr
(
D
))
tr
(
det
(
D
)
,where tr
(
D
)
and
det
(
D
)
denote the trace and the determinant of tensor D , respectively. By setting
φ 2 =
φ 1 constant, we obtain the relation for a Newtonian fluid, governed by
the Navier-Stokes equations ( 4 ). Considering
0, and
0 does not correspond to any
existent fluid under simple shear, so that the constitutive relation ( 5 ) is often used in
the reduced general form, with
φ 2 =
Moreover, respecting
the frame invariance requirements and the behavior of real fluids,
φ 2 =
0[ 21 ]:
σ = φ 0 I
+ φ 1 D
.
φ 1 becomes the
viscosity function [ 21 ], and the following general constitutive relation is obtained:
σ =
p I
+
2
μ (
II D ,
III D )
D
,
(6)
where the viscosity function
μ
might depend on the second and third invariants of D .
0 in simple shear, as well as in other viscometric flows, it is
reasonable to neglect the dependence of
Since III D =
μ
on III D .Furthermore, II D is negative
for isochoric motions, where tr
(
D
)=
0, so the positive metrics of the rate of
deformation
2 tr
γ
˙
4 II D =
(
D 2
) ,
also known as the shear rate, may be defined. Using the definition of the shear rate
as a function of the second invariant of D , relation ( 6 ) can be rewritten as follows:
σ =
p I
+
2
μ (
γ )
˙
D
.
(7)
This equation defines the constitutive equation for the generalized Newtonian fluids,
such that the equations of motion for these fluids are of the form
 
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