5.1 Initial conditions
[2333.1.1] The preceding theoretical considerations are confirmed by
numerical solutions of eq. (23) with a simple
jump-type hysteresis, as formulated in eq. (29).
[2333.1.2] The initial conditions are monotone and of the form
sz,0=Sout+SP-Sout1-Θz-z* | | (41) |
where Sout is given in Table 1.
[2333.1.3] Note that all initial conditions are monotone and
do not have an overshoot.
[2333.1.4] Two cases are, labelled A and B, will
be illustrated in the figures, namely
| SP=0.6554=S* with width z*=0.25, | | (A) |
| SP=0.9540≠S* with width z*=0.015. | | (B) |
[2333.1.5] Case A is chosen to illustrate travelling wave
solutions with cim=cdr.
[2333.1.6] The second initial condition illustrates a general overshoot
solution with two wave speeds cim≠cdr.
[2333.1.7] Moreover it illustrates one possibility for the
limit z*→0 and SP→1-SOrim in which a very
thin saturated layer (that may arise from sprinkling
water on top of the column) initiates an overshoot
profile.
[2333.1.8] This could provide a partial answer to the question of
how saturation overshoot profiles can be initiated.
5.2 Numerical Methods
[2333.2.1] The numerical solution of eq. (29)
was performed using the open source toolkit for
computational fluid mechanics Open∇FOAM [82].
[2333.2.2] This requires to develop an appropriate solver routine.
The solver routine employed here was derived from the
solver
[page 2334, §0]
scalarTransportFoam of the toolkit.
[2334.0.1] Two different discretizations of eq. (29)
have been implemented. One is based on a direct discretization of
∂fiS/∂z using the
fvc::div-operators, the other on
fi′(S)× ∂S/∂z
using fvc::grad-operators.
[2334.0.2] For the discretization of the time derivatives an
implicit Euler scheme was chosen, for the discretization
of ∂S/∂z an explicit least square scheme,
and for the discretization of the second order
term an implicit Gauss linear corrected scheme
has been selected.
[2334.0.3] The second order term had to be regularized by
replacing the function DiS with
maxS∈0,1DiS,10-3.
[2334.0.4] This avoids oscillations at the imbibition
front.
[2334.0.5] The discretized system was solved with
an incomplete Cholesky conjugate gradient solver
in Open∇FOAM .
[2334.0.6] The numerical solutions were found to differ only
in the numerical diffusion of the algorithms.
[2334.0.7] The divergence formulation seems to be numerically
more stable and accurate.
5.3 Results
[2334.1.1] Equation (38) can have
one solution, several solutions or no solution.
[2334.1.2] This can be seen numerically, but also analytically.
[2334.1.3] Depending on the values of the parameters the velocity of
the imbibition front may be larger or smaller
than that of the drainage front.
[2334.1.4] With the parameters from Table 1
the overshoot saturation for a travelling
wave as computed from (38)
is found to be S*=0.6554 and
its velocity is cdrS*=cimS*=4.2.
[2334.2.1] The travelling wave solution expected from
the graphical construction in
Figure 1a) and b)
for the initial condition A
with SP=S*=0.6554 and width z*=0.25
is displayed in Figure 1c)
at the initial time t=0 and
after dimensionless time t=0.053222 corresponding
to 4450s.
[2334.2.2] It confirms a travelling wave of the form
(36) whose velocity c*=4.2
agrees perfectly with
that predicted from eq. (38).
[2334.2.3] We have also checked that the solution does not
change with grid refinement.
[2334.3.1] For different initial conditions the numerical
solutions also agree with the theoretical considerations.
[2334.3.2] Saturation overshoot is found also when
initially a thin saturated layer with steplike or linear
profile is present.
[2334.3.3] These solutions, however, do not form travelling waves.
[2334.3.4] Instead they have cim≠cdr for their
imbibition and drainage front as predicted analytically.
[2334.3.5] For SP>S* the overshoot region grows linearly
with time at the rate cim-cdr.
[2334.3.6] Such an overshoot solution is generated by
the second initial condition B and compared with the travelling
wave solution in Figure 2.
[2334.3.7] The non-travelling overshoot for initial condition B
with z*=0.015 and SP=0.954
is shown as the solid profiles at times
t=0,0.02392,0.053222 corresponding to 0,2000,4450s.
[2334.3.8] The profile quickly approaches an overshoot
solution with plateau value S≈0.682 close
to the saturation of the Welge tangent construction.
[2334.3.9] This is higher than the plateau value S*=0.6554.
[2334.3.10] The difference will be difficult to observe experimentally
because of the large uncertainties in the measurements [54, 55].
[2334.3.11] The velocities of the numerical imbibition and drainage fronts
in the case of initial conditions B with z*=0.015 and SP=0.954
(solid curves in Fig. 2)
again agree perfectly with cim0.682=4.27 and
cdr0.682=2.813 from the theoretical analysis.
[2334.3.12] Equation (29) with initial and boundary
conditions for S and an initial condition
for ∂S/∂t is conjectured to be
a well defined semigroup of bounded operators on
L10,L on a finite interval 0,T of time.
[2334.3.13] The conjecture is supported by the fact that
each of the equations (23) individually
defines such a semigroup, and because multiplication by
Ξ or 1-Ξ are projection operators.
[2334.3.14] Equation (29) with initial and boundary
conditions for S and an initial condition
for ∂S/∂t is conjectured to be
a well defined semigroup of bounded operators on
L10,L on a finite interval 0,T of time.
[2334.3.15] The conjecture is supported by the fact that
each of the equations (23) individually
defines such a semigroup, and because multiplication by
Ξ or 1-Ξ are projection operators.
[2334.4.1] Other values of the initial saturation SP
have also been investigated.
[2334.4.2] A rich phenomenology of possibilities indicates
that the existence or nonexistence of overshoot
solutions depends very sensitively on the parameters
of the problem and the initial conditions.
[2334.5.1] Note also the asymmetric shape of the overshoot solutions
(travelling or not).
[2334.5.2] This asymmetry resembles the asymmetry seen
in experiment [54, 55].
[2334.5.3] While the leading imbibition front is steep, the
trailing drainage front is more smeared out.
[2334.5.4] This results from the capillary flux term DiS
whose values at Sout are
smaller than at Sin.