OATAO is an open access repository that collects the work of Toulouse researchers and makes it freely available over the web where possible
Any correspondence concerning this service should be sent
to the repository administrator: tech-oatao@listes-diff.inp-toulouse.fr
This is author’s version published in: http://oatao.univ-toulouse.fr/25188
To cite this version:
Guo, Jianwei and Laouafa, Farid and Quintard, Michel Sequential upscaling of multiphase dispersion in porous media. (2019) In: SITRAM 2019, Advances in the SImulation of reactive flow and TRAnsport in porous Media, 2 December 2019 - 3 December 2019 (Pau, France). (Unpublished)
Dissolution
1/24
M. Quintard
Sequential upscaling of
Sequential upscaling of
multiphase dispersion in porous
multiphase dispersion in porous
media
media
J. Guo
1, F. Laouafa
2and M. Quintard
3 1Southwest Jiaotong University, P.R. China
2
INERIS, France
3
D.R.C.E. CNRS Emeritus - Université de Toulouse (Institut de Mécanique
Dissolution
2/24
M. Quintard
Outline
Outline
Introduction to dissolution applications, Multi-scale
aspects: coupling reaction and multiphase transport?
Pore to Darcy-scale upscaling:
•
Introduction
•
Various models
•
Effective properties
Darcy-scale behavior
Large-Scale upscaling
Conclusions
Dissolution
3/24
M. Quintard
Applications...
Applications...
Karsts
Mahr and Mewes (2007)
Pet engng: CO2
storage, acid
injection, etc...
Dissolution
4/24
M. Quintard
Generic Problems: 2-phase flow
Generic Problems: 2-phase flow
lβ L β-phase averaging volume V l γ γ-phase σ-phase
Dissolution
5/24
M. Quintard
Generic Problems: Reactive
Generic Problems: Reactive
transport
transport
lβ L β-phase averaging volume V l γ γ-phase σ-phaseHomogeneous reaction
Heterogeneous reaction:
Local Equilibrium:
+ other mass balance equations
Dissolution
6/24
M. Quintard
Upscaling: momentum equations
Upscaling: momentum equations
•
Decoupling between two-phase flow and
reaction?
•
Need to neglect terms involving w
βγ
•
If ρ, μ and σ depends on concentration: need
saturation front, λS
Dissolution
7/24
M. Quintard
Model
PDEs
Quasi-static, heuristic
(Muskat)
Quasi-static, low Re, with
cross terms
Quasi-static, inertia
effects, with cross terms
More dynamic models
(transient terms,
“pseudo-functions”, ...)
Decoupled momentum transfer:
Decoupled momentum transfer:
various models
Dissolution
8/24
M. Quintard
...cont.: hybrid models, N-eqs
...cont.: hybrid models, N-eqs
models
models
Trickle Bed (X-ray, IFP)
Mahr and Mewes (2007)
Phase
“splitting”
→ N-eqs
(Soulaine et al., 2014;
Pasquier, 2018)
PNM with
dynamic
laws!
Dissolution
9/24
M. Quintard
Upscaling Dispersion → various models!
Upscaling Dispersion → various models!
1D Macro-Scale
{
DNS
1-eq local equilibrium
2-equation, N-equation
rate or MRMT, ...
Mixed or Hybrid models
meso-scale Network model
Mixed or Hybrid Network
model (PNM+VOF)
3D µ-scale
1-eq non-eq: convolution,
asympt. 2-eq, frac. deriv.,
wave eq., CTRW,...
Mixed or Hybrid models
for front problems
Classical
dispersion
Dissolution
10/24
M. Quintard
Active Dispersion: specific
Active Dispersion: specific
aspects
aspects
•
Impact of n.w
•
Tortuosity and
dispersion ≠ from
passive dispersion
•
Effective reaction rate
•
Convective correction
(“drift”)
•
Importance of
non-local effects
This talk → mainly
trapped phase
●2-φ VOF,
etc..
●PNM
●Large-scale
Dissolution
11/24
M. Quintard
Fully coupled micro-macro model with
Fully coupled micro-macro model with
“n.w” terms
“n.w” terms
dispersion
tortuosity
I.
II.
III.
IV.
V.
specific area:
+
Dissolution
12/24
M. Quintard
Macro-scale model and effective
Macro-scale model and effective
parameters (simplified closure, no n.w)
parameters (simplified closure, no n.w)
“Effective reaction”:
Mass exchange term:
Dispersion tensor ≠ from passive dispersion:
Additional convective terms:
Dissolution
13/24
M. Quintard
Effective “reaction rate” (ex.: linear reaction
Effective “reaction rate” (ex.: linear reaction
rate)
rate)
Pore-scale Damkhöler number:
Note: if
y
s lx
H/2 R 0Purely transport limited =
Local Non-Equilibrium Model
0 0.2 0.4 0.6 0.8 1 10-3 10-2 10-1 100 101 102 103 104 Da
= .2
.5
.9
Dissolution
14/24
M. Quintard
Dispersion
Dispersion
10-1 100 101 102 103 100 101 102 103 104 n=1, D a=1 n=3 n=5 n=1, D a=100 n=3 n=5 n=1, D a=1 n=3 n=5 n=1, D a=100 n=3 n=5Pe
n=1, D a=1 n=3 n=5 n=1, D a=100 n=3 n=5l i
s
l
s
s
l
i
Da=0 → passive case
Da → ∞ → uniform equil. conc. at A
βσ
Guo et al.,
2015
Dissolution
15/24
M. Quintard
Importance of non-local effects
Importance of non-local effects
and drift
and drift
fluid/solid repartition
fluid concentration
fluid x-velocity
h
0y
x
L
H
h ( x , t )
Comparison with 1D averaged model
Note: need additional “convective” terms
Hyp.: Re~0 Darcy , Ra=0
Improvements: use of non local effective parameters...
...or hybrid formulations!
Entrance effects
D
N
S
Dissolution
16/24
M. Quintard
Darcy-Scale → Large-Scale
Darcy-Scale → Large-Scale
ω η lω lηl
d dissolution frontL
pore soluble insoluble pore soluble insoluble1
stupscaling
Pore-scale model
Darcy-scale model
Large-scale model
DNS
2
ndupscaling
α=s,i,l
s : soluble phase
i: insoluble material
l: liquid phase (water + dissolved
species)
Dissolution
17/24
M. Quintard
Darcy-scale model (ex.: gypsum)
Darcy-scale model (ex.: gypsum)
l
η R0 L ω ηl
ω ∞ s l ir
0 ll ls liDarcy-scale
Pore-scale
Large-scale?
Damköhler number
Dissolution
18/24
M. Quintard
Dissolution of heterogeneous
Dissolution of heterogeneous
systems: scale separation?
systems: scale separation?
x C x C 10.+4 10.-5 10.-4 10.-3 10.-2 10.-1 10.+0 10.+1 10.+2 10.+3 10.-4 10.-3 10.-2 10.-1 10.+0 10.+1 10.+2 10.+3 Conical Wormhole Dominant Wormhole Ramified Wormhole Uniform Compact