Geology Reference
In-Depth Information
of the overlying plate. This is a consequence of
a fundamental empirical law of fluid dynamics
that is known as
no
-
slip boundary condition
(e.g.,
Pozrikidis
2009
), which states that in a fluid the
tangential component of the velocity field is con-
tinuous across a solid boundary. Accordingly, the
average strain rate through a cross-section of the
fluid sheet in Fig.
13.1
will be:
P
©
D
v
=h.If£ is
the shear stress that the overlying plate exerts on
the fluid, then the total force is
F
D
£
A
, thereby
the power dissipated by shearing is: W
D
F
v
D
£Ah
P
©
D
£V
P
©. In general, the power dissipated
in a fluid by viscous deformation is referred to
as
viscous dissipation
and is associated with an
irreversible conversion of mechanical energy into
temperature increases.
If
w
is the work per unit volume associated
with the viscous flow, than the viscous dissipation
function, ˆ, has the expression:
The rate of change of the kinetic energy can be
obtained taking the total derivative of the volume
then the material derivative of the volume integral
of § over a region
R
is given by:
Z
Z
d
dt
C
§.r;t/
r
v
dV
d
dt
§.r;t/dV
D
R
R
Z
@§
@t
C
@x
i
.§
v
i
/
dV
@
D
(13.23)
R
Therefore, using the continuity Eq. (
13.7
), for
the kinetic energy we obtain:
Z
Z
d
dt
1
2
K
D
¡
v
2
dV
D
¡
v
k
P
v
k
dV (13.24)
R
R
Let us consider now the internal energy
U
,
which can be written as follows:
@
v
i
@x
j
ˆ
D
w
D
£
0
ij
(13.20)
Z
U.t/
D
¡.r;t/
u
.r;t/dV
(13.25)
where £
0
is the deviatoric stress tensor. Substi-
tuting the deviatoric part of expression (
13.14
)
gives:
R
where
u
is the internal energy per unit mass.
Using (
13.23
) we obtain for the rate of change
of the internal energy:
ǜ
@
v
i
@x
k
•
ij
@
v
i
@
v
j
@x
i
C
œ
@
v
k
ˆ
D
@x
j
C
@x
j
(13.21)
d
dt
.¡
u
/
C
¡
u
r
v
dV
Z
Z
d
dt
U
D
¡
u
dV
D
R
R
Therefore, both dynamic and second viscosities
lead to dissipation in a fluid. Now we are ready
to formulate the law of energy conservation for a
fluid parcel. Differently from the heat diffusion
account of the advection of material, thereby the
partial derivative of the temperature will be sub-
stituted by a material derivative. In general, the
conservation of energy of a mass of fluid requires
that the rate of change of the kinetic energy, K,
plus the rate of change of the internal energy, U ,
be equal to the mechanical power input, W ,plus
the rate of heat produced within or entering the
body, Q:
Z
Z
D
Œ
u
P
¡
C
¡
P
u
C
¡
u
r
v
dV
D
¡
P
u
dV
R
R
(13.26)
The total energy content of the region of fluid
R
may change as a consequence of flow through
its surface
S
(
R
), heat conduction, work done by
the gravity field or by surface tractions, and ra-
dioactive heat production. The mechanical power
input arises from surface forces applied along
S
(
R
) and from the gravity force exerted on each
volume element in
R
. Let us consider first the
surface force exerted on a surface element
dS
with orientation
n
.If
T
(
n
) is the traction, then the
power input on
dS
is given by:
K
C
U
D
W
C
Q
(13.22)