Civil Engineering Reference
In-Depth Information
l
2
r
2
r
1
l
1
Figure 5.3
A pore made up of an alternating sequence of cylinders.
As far as the macroscopic velocity is considered, the nonviscous fluid must be replaced
by a fluid of density
ρ
0
α
∞
. The value of the tortuosity is an intrinsic property of the
porous frame that depends on the micro-geometry. When the saturating fluid is vis-
cous the effective density must tend to
α
∞
ρ
0
when the viscous skin depth tend to zero
and the viscosity effects become negligible. For the material of Sections 4.9 and 4.10,
α
∞
=
1
/
cos
2
ϕ
in the direction perpendicular to the surface of the layer. A tortuosity
larger than 1 is due to the dispersion of the microscopic velocity in Equation (5.21). This
dispersion can be created by variations of the diameter of the pores. Let us consider, for
instance, a material with identical pores parallel to the direction of propagation, made up
of alternating cylinders represented in Figure 5.3, with lengths
l
1
and
l
2
and cross-sections
S
1
and
S
2
, respectively. Even if the fluid is nonviscous, the description of the inertial
forces and the evaluation of
α
∞
by Equation (5.21) are very complicated at the junction
of the two cylinders. A simple approximation is obtained by assuming constant veloci-
ties in each cylinder. It is shown in Appendix 5.A that with this approximation,
α
∞
is
given by
(l
1
S
2
+
l
2
S
1
)(l
1
S
1
+
l
2
S
2
)
α
∞
=
(5.23)
l
2
)
2
S
1
S
2
(l
1
+
The evaluation of tortuosity can be performed from resistivity measurements, as indi-
cated in Section 4.9. Another method simultaneously allowing the measurement of other
high-frequency parameters is described at the end of Section 5.3.5.
5.3.2 Viscous characteristic length
For materials with cylindrical pores, as indicated by Equations (4.107) and (4.155), the
high-frequency behaviour of
ρ
and
K
depends on tortuosity and on the hydraulic radius.
The viscous characteristic length defined by Johnson
et al
. (1986) replaces the hydraulic
radius for more general micro-geometries. Johnson
et al
. have defined the characteristic
dimension
by
A
υ
i
(
r
w
)
d
A
2
=
V
υ
i
(
r
)
d
V
(5.24)
For a static flow of nonviscous fluid in the porous structure,
υ
i
(
r
w
)
is the velocity of
the fluid on the pore surface and the integral in the numerator is performed over the pore