[2328.2.1] Infiltration experiments [59] on constant flux imbibition into a very dry porous medium report existence of non-monotone travelling wave profiles for the saturation [55, 62]
(20) |
as a function of time
(21) |
and the parameter
(22a) |
defines the dimensional depth coordinate
(22b) |
where
(22c) |
[2328.2.8] Experimental observations show fluctuating profiles with an overshoot region [59, 73, 54, 55, 74, 75]. [2328.2.9] It can be viewed as a travelling wave profile consisting of an imbibition front followed by a drainage front.
[2328.3.1] The problem is to determine the height
[2328.4.1] The leading (imbibition) front is a solution of the nondimensionalized
fractional flow equation (obtained from eq. (17) for
(23) |
[page 2329, §0] while
(23) |
must be fulfilled at the trailing (drainage) front.
[2329.0.1] Here
(24a) | |||
(24b) |
with
(25) |
defined in terms of total flux
(26) |
with
(27) |
is the macroscopic capillary number [76, 37]
with
(28) |
for the leading (imbibition) front and
(28) |
for the trailing (drainage) front.
[page 2330, §1]
[2330.1.1] Conventional hysteresis models for the traditional theory require to store the process history for each location inside the sample [77, 78, 79]. [2330.1.2] Usually this means to store the pressure and saturation history (i.e. the reversal points, where the process switches between drainage and imbibition). [2330.1.3] A simple jump-type hysteresis model can be formulated locally in time based on eq. (23) as
(29) |
[2330.1.4] Here
(30) |
(31a) | |||
(31b) |
with
(32) |
the effective saturation. [2330.1.6] The resulting fractional flow functions with parameters from Table 1 are shown in Figure 1b. [2330.1.7] The capillary pressure functions used in the computations are
(33) |
with
(34) |
[2330.1.8] Equation (29) with initial and boundary
conditions for