solute injection
TRANSCRIPT
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 1/10
© COPYRIGHT 2008. All right reserved. No part of this documentation may be photocopied or reproduced in
any form without prior written consent from COMSOL AB. COMSOL, COMSOL Multiphysics, COMSOL Reac-
tion Engineering Lab, and FEMLAB are registered trademarks of COMSOL AB. Other product or brand names
are trademarks or registered trademarks of their respective holders.
Solute InjectionSOLVED WITH COMSOL MULTIPHYSICS 3.5a
®
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 2/10
S O L U T E I N J E C T I O N | 1
S o l u t e I n j e c t i o n
Introduction
Predicting the transport of contaminants that move with subsurface fluids generally
means analyzing at least two physics. This model tracks a contaminant that enters an
at a point, such as an injection well or toxic spill, and spreads through the aquifer with
time. The model has an analytic solution developed by Wilson and Miller (Ref. 1),
which has been used to test several dedicated fluid flow and transport codes. The
particular problem in this model comes from the MT3DMS manual of Zheng and
Wang (Ref. 2).
The analysis models steady-state fluid flow and follows up with a transient
solute-transport simulation; it employs the Darcy’s Law application mode and the
Solute Transport application mode from the Earth Science Module. In COMSOL
Multiphysics it is straightforward to specify a fluid velocity without solving a flow
problem. This example solves for the velocities to demonstrate the mechanics of
coupling flow and transport simulations in one model file.
The example also shows how to use the solver settings for the combined steady-state
and transient solution. The instructions detail how to model a point source using the
point flux settings available in the Earth Science Module.
The first section in this discussion gives an overview of the problem. Next it gives the
equations and describes how the fluid flow and the solute transport application modeslink in COMSOL Multiphysics. Next come a few implementation details including a
table of model data. The results shown next then illustrate various postprocessing
options. The last section describes how to build the model using the COMSOL
Multiphysics graphical user interface.
Model Definition
In this example, there is regional flow from left to right across a 450 m-by-300 m
aquifer. The fluid moves at a Darcy velocity of 0.11 m/d. The aquifer has
homogeneous and isotropic material properties. A point source releases a small
amount of fluid into the aquifer at 1 m3/d, a release rate small enough for the flow
field to remain uniform. The injected fluid carries a nonreactive solute at a
concentration of 1000 ppm. The contaminant migrates by advection and dispersion
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 3/10
S O L U T E I N J E C T I O N | 2
and never reaches a boundary. The aquifer is initially pristine with concentrations
everywhere equal to zero. The only source of contaminant is the injection, so flow
through the inlet has zero concentration. The period of interest is one year.
F L U I D F L O W
Darcy’s law describes the fluid flow in this problem. With the hydraulic-head
formulation, the governing equation is
where K is hydraulic conductivity (m/d), H is hydraulic head (m), and Qs is the volume flow rate of fluid per unit volume of aquifer (d−1).
The point source is
where W is the volumetric pumping rate W (m3/d); b is the aquifer thickness (m); and
δ denotes the Dirac delta function, which is nonzero only in the point ( xi, yi), where xi and yi are the well coordinates.
Because the flow field is at steady state, you can obtain a unique solution by specifying
the model geometry, the point source, the material properties, and the boundary
conditions. The problem statement gives the hydraulic head at the inlet and the outlet
and indicates symmetry conditions on the sides. In the Darcy’s Law application mode,
you express these boundary conditions as
where n is the unit vector normal to the boundary.
C O U P L I N G
The groundwater-flow and solute-transport equations given here are linked by the
Darcy velocity, , which gives the specific flux (m/d) of fluid across an
infinitesimal surface representing both the solids and the pore spaces. COMSOL
Multiphysics computes the Darcy velocity vector u, which consists of the x and y
directional velocities denoted by u and v, respectively.
∇ K ∇ H –( )⋅ Qs
=
Qs
W
b-----δ x xi y yi–,–( )=
n K ∇ H ( )⋅ 0= ∂Ω Sides
H H in
= ∂Ω Inlet
H 0= ∂Ω Outlet
u K ∇ H –=
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 4/10
S O L U T E I N J E C T I O N | 3
S O L U T E T R A N S P O R T
The advection-dispersion equation governs solute transport in this problem:
Here D L is the hydrodynamic dispersion tensor (m2/d); θs denotes the fluid volume
fraction; c gives the dissolved concentration (kg/m3); u is the Darcy velocity (m/d);
and Sc represents the quantity of solute added per unit volume of porous medium per
unit time (kg/(m3·d)).
The entries for the dispersion tensor are
where D Lii are the principal components of the dispersion tensor; D Lij are the cross
terms; α represents the dispersivity (m); and the subscripts “1” and “2” denote
longitudinal and transverse flow, respectively.
In this problem, Sc represents the solute injected at the point well, which is defined by
where cQ is the concentration of the solute in the water (kg/m3). You implement the
solute injection with the same logic as the fluid point source.
The problem statement specifies that the only contaminant source in the aquifer is the
point well, and that the boundaries far enough from the injection well for the
contaminant never to leave the model domain. You thus set the inlet concentration to
zero and assign the other boundaries an advective flux. The expressions for these
boundary conditions are
where n is the unit vector normal to the boundary.
θs
c∂
t∂----- ∇ θ
s– D L c uc+∇( )⋅+ S
c=
θ D Li i α1
ui2
u
------- α2
u j2
u
-------+=
θ D Li j θ D Lj i α1
α2
–( )uiu
j
u
-----------= =
Sc
Qs
cQW
b-----cQδ x xi y yi–,–( )= =
n θs
– D L c∇( )⋅ 0= ∂Ω Sides
c 0= ∂Ω Inlet
n θs
– D L c∇( )⋅ 0= ∂Ω Outlet
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 5/10
S O L U T E I N J E C T I O N | 4
Model Data
Build the model with the following data:
PARAMETER NAME VALUE
K Hydraulic conductivity 1 m/d
ρf Fluid density 1000 kg/m3
g Gravity 9.82 m/s2
u Darcy velocity 0.11 m/d
W Pumping rate 1 m3/d
b Aquifer thickness 10 m
H in Inlet head 45 m
θs Porosity 0.3
α1 Longitudinal dispersivity 10 m
α2 Transverse horizontal dispersivity 3 m
cs Solute concentration at source 1000 ppm
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 6/10
S O L U T E I N J E C T I O N | 5
Results
Figure 1 shows the solution to the steady-state flow problem. The hydraulic headdrops from the inlet to the outlet, and the velocity field is almost uniform, as required
in the problem statement (Ref. 1).
Figure 1: COMSOL Multiphysics solution of almost uniform Darcy flow in a domain with a small point leak. Shown are the hydraulic head (surface plot) and velocity field (arrows).
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 7/10
S O L U T E I N J E C T I O N | 6
Figure 2: COMSOL Multiphysics results for th e solute-transport problem are a near perfect matc h to th e analytic solution of Ref. 1, which is shown with the numerical estimates of Ref. 2 .
Figure 3 illustrates the evolution of the contaminant plume with snapshots at 30 days,
100 days, and 360 days. The solute plume spreads with time but never reaches the
boundary. In creating these plots, the author clipped off concentrations below
0.1 ppm and used an expression containing logical operators to give the same shading
to zones with concentrations of 50 ppm or greater.
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 8/10
S O L U T E I N J E C T I O N | 7
Figure 3: Concentrations at 30 days (top left), 100 days (top right), and 360 days (bottom) for 2D fluid flow and solute transport for a continuously injecting point source; shown are concentrations from 0.1 ppm to 50 ppm or greater.
In the user interface you can interactively view the value at a given point by either
clicking at the point of interest or entering the point coordinates to trigger a numeric
readout. You can also obtain numeric results for the arbitrary expressions along a line
or within a subdomain using cross-section and domain plots. The cross sections in
Figure 4 and Figure 5, for example, illustrate the advective and dispersive components
of the solute flux. The flux from chemical diffusion is zero. The COMSOL
Multiphysics solution shown here gives results along the line y = 150 m at 10, 30, 90,
180, and 360 days.
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 9/10
S O L U T E I N J E C T I O N | 8
Figure 4: Advective flux along y = 150 m at 10, 30, 90, 180, and 360 days.
Figure 5: Dispersive flux along y = 150 m at 10, 30, 90, 180, and 360 days.
7/27/2019 Solute Injection
http://slidepdf.com/reader/full/solute-injection 10/10
S O L U T E I N J E C T I O N | 9
Figure 6 gives the solute concentration as a combined color and height plot.
Figure 6: Solute concentrations from 0.1 ppm to 50 ppm at 360 days.
References
1. J.L. Wilson and P.J. Miller, “2D plume in uniform ground-water flow,” J. Hyd.
Div., ASCE , vol. 4, pp. 503–514, 1978.
2. C. Zheng and P. Wang, MT3DMS: A Modular Three-Dimensional Multispecies
Transport Model for Simulation of Advection, Dispersion and Chemical Reactions
of Contaminants in Groundwater Systems , University of Alabama, 1998.