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d W D T .n/ v dS D v i ij n j dS
D ij v j n i dS D v / dS
@ v j
@x i C k r
2 T C ¡ H
¡ P u D £ ij
(13.31)
(13.27)
The first term at the right-hand side of ( 13.31 )
can be expressed in terms of viscous dissipation
function and pressure power input. In fact, by the
symmetry of the stress tensor we have that:
where we have applied Cauchy's theorem ( 7.3 )
and the symmetry condition ( 7.2 ) for the stress
tensor. Therefore, using Gauss' theorem (see Ap-
pendix I) we see that the power done by surface
forces on S ( R ) is given by:
p• ij C £ 0 ij @ v i
@x j
@ v j
@x i D £ ji
@ v j
@x i D £ ij
@ v i
@x j D
£ ij
I
Z
W D
v / dS D
r v /dV (13.28)
D p @ v k
@x k C ˆ
(13.32)
S. R /
R
Therefore, the conservation law ( 13.31 ) can be
rewritten as follows:
The total mechanical power on R is then
calculated as follows:
Z
2 T C ¡H (13.33)
¡ P u D p r v C ˆ C k r
W D
Œ r v / C ¡g v dV
The internal energy density u in ( 13.33 )is
not independent from the temperature T and the
pressure p , thereby it is useful to find a form of the
energy conservation law such that u is substituted
by an expression of T and p . To this purpose,
we can use the first law of thermodynamics,
which states that in absence of mass exchange
the infinitesimal variation of internal energy, du ,
of a region is the sum of the energy per unit
mass absorbed in the from of heat, • q ,andthe
infinitesimal work done by the surrounding on the
system, • w :
R
ij
@x i C ¡g j v j dV
Z
@x i v j C £ ij @ v j
D
R
Z
@ ij
@x i C ¡g j v j C £ ij @ v j
dV
D
@x i
R
jk
@x k C ¡g j v j C £ ij
dV
Z
@ v j
@x i
D
R
Z
dV
P v j v j ¡ C £ ij @ v j
@x i
D
(13.29)
R
d u D •q C w
(13.34)
where we have used the Lagrangian version of
the equations of motion ( 13.10 ). Finally, the heat
power associated with the heat flow q into R
and with the radiogenic heat H can be obtained
easily generalizing ( 12.10 ) through inclusion of
the contribution of H :
Although irreversible processes occur in
a fluid, for example viscous dissipation, a
simple expression for du can be obtained only
assuming that the transformation is quasi-static
(i.e., reversible), thereby frictional heating and
other irreversible processes are considered of
secondary importance. In this hypothesis, the
first law of thermodynamics can be rewritten as
follows:
Z
k r
2 T C ¡H dV
Q D
(13.30)
R
The energy balance and conservation law can
be formulated by substituting the expressions
( 13.24 ), ( 13.26 ), ( 13.29 ), and ( 13.30 )into( 13.22 )
and taking into account that the equation holds for
any arbitrary region R . Therefore:
d u D •q pd
(13.35)
where D 1/¡ is the specific volume (volume per
unit mass). The heat per unit mass adsorbed by
the system can be expressed as follows:
 
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