Abstract:
Miscible displacement flows in porous media are of significant importance in many
industrial, environmental, and engineering applications, such as enhanced oil recovery,
chromatography separation, CO2 sequestration, contaminant transport in geological
aquifers, etc. These displacement flows feature different hydrodynamic instabilities
depending on the physical properties of the fluids involved and the characteristics
of the porous media. In this thesis, we numerically analyze the stability of miscible
displacement flows in a homogeneous porous medium. To mathematically model
such displacement flows and their stability analysis we assume that the fluids are
incompressible, neutrally buoyant, and nonreactive. The fluid viscosity is determined
by the presence of a solute concentration dissolved in the solvent.
Viscous fingering (VF) is observed when a less viscous fluid displaces a more viscous
one in porous media. Perturbations at the fluid-fluid interface protrude, and
the more mobile displacing fluid invades through the less mobile resident fluid. Thus,
the interface develops finger-like projection at the interface, hence called viscous fingering.
The mathematical challenges of a linear stability analysis (LSA) of miscible
VF are due, mainly, to the time-dependent base-state flow. These problems feature
two different time scales: (a) diffusive-time scale for the evolution of the base state
and (b) time scale for the evolution of the perturbations. Over the last few decades’
quasi-steady-state approximation (QSSA) method has been extensively used to characterize
the stability in the linear regime. However, QSSA method fails to successfully
capture the onset of instability. In this direction, this thesis develops a new linear
stability technique, in the similarity transformation domain based on the principle of
QSSA method, and abbreviated as SS-QSSA.
SS-QSSA successfully captures the onset of instability in miscible VF. SS-QSSA is
further used to characterize the stability of a finite fluid slice of more or less viscosity
than the displacing fluid. Numerically we have proved the existence of a critical
sample width for the onset of instability, and also computed the critical sample width for different flow conditions. Dispersion of the solute is a very essential phenomenon
that characterizes the stability of a miscible system. The influence of the solute
dispersion on the stability of miscible displacements is analyzed numerically in terms
of a dimensionless parameter, the P´eclet number.
Steep concentration gradient in miscible system results a nonconventional stress,
called the Korteweg stress. The existence of this stress in various mixtures, such
as water-glycerine, isobutyric acid-water, water-honey, etc., has been experimentally
verified. We analyze the influence of the Korteweg stress on miscible VF. It is shown
that the Korteweg stress has a stabilizing influence, which is ensured from the delayed
onset of instability measured using SS-QSSA. Critical sample width increases with
the Korteweg stress strength. For a given sample size larger than its critical value,
instability region shrinks with the strength of the Korteweg stress. Counterintuitive
results, the instability enhances with the increasing magnitude of the Korteweg stress,
are observed for very large P´eclet values.
Numerical simulations of the complete nonlinear problem are performed using a
Fourier pseudospectral method to capture the nonlinear dynamics and pattern formation.
We showed that the Korteweg stress inhibits the tip-splitting phenomenon,
which is important in miscible flow because it increases the contact between fluids,
thus enhancing mixing and reaction rates. The inhibition of tip-splitting instability
in the presence of these stresses signifies that the Korteweg stress is analogous to the
surface tension in immiscible fluids. The growth rate and the wave number of the
unstable modes obtained from our nonlinear simulations are in excellent agreement
with those obtained from self-similar LSA.
Through nonlinear simulations, we have determined three different instability
modes of a more viscous circular sample in rectilinear displacement in homogeneous
porous media. It is shown that there exists a finite window of log-mobility ratio for
VF in a more viscous circular blob, which is completely new in miscible viscous fingering.
On the other hand, for a less viscous blob comet shape deformation is observed
for viscosity contrasts larger than a critical value. In this case, fingering instability
enhances as the viscosity contrast increases beyond the critical value.
A linear stability tool is also developed using the same Fourier pseudospectral
method used for the nonlinear simulations. This linear stability method is more
generic, computationally rigorous but less expensive, and also mathematically robust.
Using this tool and a new viscosity scaling we determine the onset of instability in
a finite slice of more of less viscosity than the displacing fluid in the presence of the
Korteweg stress. It is shown that the instability sets in at the same time both in a less viscous and a more viscous finite slice. Nonlinear simulations support our LSA
results. This linear stability technique can be helpful for any hydrodynamic instability
problem with unsteady base state.
Influence of viscosity contrast on buoyantly unstable miscible layer in vertical
porous media is analyzed through nonlinear simulations. It is shown that the viscosity
contrast acts against the Rayleigh-Taylor instabilities in vertical porous media.
However, when one fluid displaces the other, instability enhances as the viscosity
increases with the depth.
The findings of this thesis will be helpful for understanding the fluid mechanics
aspects inherent in the problems of chromatographic separation, oil recovery, contaminant
transport, and geological CO2 sequestration.