Environmental Engineering Reference
In-Depth Information
Then (4.10) leads to the following relationship between pressure and temperature
p
D
NT
.
(4.12)
Equation (4.12) is the equation of state for an ideal gas.
4.1.3
The Navier-Stokes Equation
Note that above in deriving the generalized Euler equation (4.6) for a one-compo-
nent system we ignored collisions between atoms, and collisions between atoms
or molecules of different components are taken into account in (4.7)-(4.9) through
typical times
qs
. We now include collisions between atoms in the balance equation
for the average atom momentum for a one-component system. Such collisions lead
to the frictional force between neighboring gas layers which are moving with dif-
ferent velocities. This effect is expressed through the gas viscosity coefficient
τ
,
which is taken into account as arising from the above-mentioned frictional force.
According to the definition of the viscosity coefficient
η
, if a gas (or liquid) is mov-
ing along the
x
-axis and varies in the
z
direction, the frictional force
f
per unit area
is given by
η
D
η
@
w
x
@
f
,
(4.13)
z
where
w
x
is the average gas velocity.
We include the gas viscosity in the expression for the pressure tensor, which
takes the form
P
0
α
,
where the latter term accounts for the gas viscosity. On the basis of the viscosity
definition and transferring to an arbitrary frame of reference, one can represent
the pressure tensor
P
0
α
P
α
D
p
δ
α
C
, which is symmetric, in the form
@
.
w
α
@
x
C
@
w
@
δ
α
@
w
α
@
P
0
α
D
η
x
α
C
a
x
The factor
a
may be found as follows. The forces of viscous friction in a gas occur
because neighboring gas layers move with different velocities. If a gas could be
decelerated as a whole, this friction mechanism would have no effect and the force
due to the gas viscosity would vanish. Hence, the trace of the pressure tensor is
zero. This yields
a
D
2/3, and the viscosity term in the pressure tensor can be
writtenintheform
@
.
w
α
@
x
C
@
w
@
2
3
δ
α
@
w
α
@
P
0
α
D
η
x
α
(4.14)
x
With the viscosity part of the pressure tensor taken into account, (4.4) takes the
form of the Navier-Stokes equation [6-10]:
@
w
@
C
ν
Δ
w
C
3
r
w
C
m
,
p
(
w
r
)
w
D
r
t
C
(4.15)