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We investigate the flow-channeling phenomenon caused by thermal drawdown in fractured geothermal reservoirs. A discrete fracture network-based, fully coupled thermal–hydrological–mechanical simulator is used to study the interactions between fluid flow, temperature change, and the associated rock deformation. The responses of a number of randomly generated 2D fracture networks that represent a variety of reservoir characteristics are simulated with various injection-production well distances. We find that flow channeling, namely flow concentration in cooled zones, is the inevitable fate of all the scenarios evaluated. We also identify a secondary geomechanical mechanism caused by the anisotropy in thermal stress that counteracts the primary mechanism of flow channeling. This new mechanism tends, to some extent, to result in a more diffuse flow distribution, although it is generally not strong enough to completely reverse flow channeling. We find that fracture intensity substantially affects the overall hydraulic impedance of the reservoir but increasing fracture intensity generally does not improve heat production performance. Increasing the injection-production well separation appears to be an effective means to prolong the production life of a reservoir.
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ORIGINAL PAPER
Thermal Drawdown-Induced Flow Channeling in Fractured
Geothermal Reservoirs
Pengcheng Fu
1
Yue Hao
1
Stuart D. C. Walsh
1
Charles R. Carrigan
1
Received: 31 March 2015 / Accepted: 1 June 2015 / Published online: 30 June 2015
Springer-Verlag Wien (outside the USA) 2015
Abstract We investigate the flow-channeling phe-
nomenon caused by thermal drawdown in fractured
geothermal reservoirs. A discrete fracture network-based,
fully coupled thermal–hydrological–mechanical simulator
is used to study the interactions between fluid flow, tem-
perature change, and the associated rock deformation. The
responses of a number of randomly generated 2D fracture
networks that represent a variety of reservoir characteris-
tics are simulated with various injection-production well
distances. We find that flow channeling, namely flow
concentration in cooled zones, is the inevitable fate of all
the scenarios evaluated. We also identify a secondary
geomechanical mechanism caused by the anisotropy in
thermal stress that counteracts the primary mechanism of
flow channeling. This new mechanism tends, to some
extent, to result in a more diffuse flow distribution,
although it is generally not strong enough to completely
reverse flow channeling. We find that fracture intensity
substantially affects the overall hydraulic impedance of the
reservoir but increasing fracture intensity generally does
not improve heat production performance. Increasing the
injection-production well separation appears to be an
effective means to prolong the production life of a
reservoir.
Keywords Geothermal Enhanced geothermal system
Hot wet rock Thermal breakthrough Flow channeling
THM model
1 Introduction
Engineered (or enhanced) geothermal systems (EGS) are
usually located in fractured rock formations, where the
permeability of the intact rock matrix is very low and the
inter-connected fracture network provides the primary
conduit of fluid between the injection well(s) and the
production well(s). Since heat conduction in the rock
matrix is much slower than convective heat transfer asso-
ciated with fluid flow along fractures, it is highly desirable
to have flow patterns dispersed throughout a large volume
of rock. The understanding of flow patterns in EGS reser-
voirs plays a critical role in the optimization of reservoir
exploration, stimulation, and operation.
The term ‘‘flow channeling’’ generally refers to con-
centration of the flow network in a relatively small number
of ‘‘flow channels’’ or ‘‘flow pathways’’, as opposed to
evenly dispersed flow in the medium. In the context of flow
in fractured media, its meanings are manifold. When fluid
flow along a given single fracture is concerned, ‘‘flow
channeling’’ is used to describe the distinctive linear
channels forming along this planar fracture (Tsang and
Tsang 1987; Tsang and Neretnieks 1998; Auradou et al.
2006). In the reservoir scale involving a network of frac-
tures, ‘‘flow channeling’’ refers to a flow pattern in which a
small portion of the fractures carry the majority of the fluid
flow. The primary reason for channelized flow in these two
cases is the heterogeneous spatial distribution of fracture
transmissivity, along a given fracture plane and within the
fracture network, respectively. ‘‘Flow channeling’’ also
refers to the process through which a channelized flow
pattern forms or evolves due to various mechanisms.
The present study focuses on the evolution of flow
channeling at the reservoir scale associated with thermal
drawdown in EGS. An intuitive mechanism for this process
&Pengcheng Fu
fu4@llnl.gov
1
Atmospheric, Earth, and Energy Division, Lawrence
Livermore National Laboratory, Livermore, CA 94550, USA
123
Rock Mech Rock Eng (2016) 49:1001–1024
DOI 10.1007/s00603-015-0776-0
is illustrated in Fig. 1as follows: at the commencement of
the production phase of an EGS (before significant thermal
drawdown has taken place), the flow pattern from the
injection well(s) to the production well(s) is likely to be
somewhat channelized, owing to the inherent heterogeneity
of the fracture system (i.e. the second phenomenon descri-
bed in the previous paragraph). The thicker and thinner lines
in Fig. 1a represent flow paths with higher and lower flow
rates, respectively. During heat production, fractures that
carry higher flow rates are likely to cool faster. Thermal
stress in the cooled rock (the blue zone in Fig. 1b) is typi-
cally a tensile increment in addition to the original com-
pressive in situ stress. It tends to reduce the magnitude of
the total compressive stress on fractures inside the cooled
rock, thereby increasing the permeability along these frac-
tures. Therefore, a likely scenario is that flow will further
concentrate in these cooled fractures and diminish in others
as shown in Fig. 1b. This is undesirable for EGS because it
reduces the effective heat exchange area of the reservoir and
undermines long term thermal performance. This mecha-
nism has been demonstrated by numerical models, such as
those in Hicks et al. (1996), DuTeaux et al. (1996), and Koh
et al. (2011). It has been observed in several EGS projects
that the overall flow impedance between the injection and
production wells decreases with heat production (Kohl et al.
1995), which could be a manifestation of the hypothetical
mechanism. However, tracer tests at the Fenton Hill EGS
site indicated that the flow pattern became more diffuse at
certain stages of the heat production operation (DuTeaux
et al. 1996). Flow channeling, particularly the mechanisms
of flow channeling, in EGS during heat production deserves
further investigation.
The phenomenon to be studied herein entails coupled
mechanical, hydrological, and thermal processes. Hence,
the numerical model must simulate all the three aspects of
the problem and their coupling. Various coupled thermal–
hydrological–mechanical (THM) models and models cou-
pling two of the three aspects for geothermal reservoirs
have been developed and reported in the literature. Models
for conventional geothermal resources, namely hydrother-
mal systems dominated by flow in porous rock formations,
typically handle fluid and heat flow using porous medium
flow theories (see a review in O’Sullivan et al. 2001).
Mechanical coupling capability can be added to these
models through rock constitutive models based on contin-
uum mechanics, which quantifies the stress–strain rela-
tionship of the porous medium (Hart and St. John 1986;
Rutqvist et al. 2002; Taron et al. 2009; Taron and Elsworth
2009). For EGS reservoirs dominated by flow in fractures,
the porous medium models have been found to be inade-
quate (Nicol and Robinson 1990), and explicit represen-
tation of the fracture system is necessary. A number of
models in the literature focus on the flow and deformation
of a single fracture. Such models could be useful for
reservoirs that are dominated by a single fracture (Bo
¨d-
varsson and Tsang 1982; Ghassemi et al. 2007). Several
coupled THM models based upon discrete fracture network
(DFN) flow have been developed. The early models usually
handle simple fracture network patterns whereas the more
advanced ones can deal with random fracture networks.
Many complex and interesting phenomena in EGS reser-
voirs have been revealed by the application of these
models, but a comprehensive study of thermal drawdown-
induced flow channeling is still missing.
Fig. 1 Conceptual illustration
of the flow channeling concept
in an idealized fracture network:
athe flow field in the initial
state, and bthe flow field after a
cooled zone has developed due
to heat production. The solid
arrowed line represents flow
paths with the flow rate denoted
by the line thickness
1002 P. Fu et al.
123
We present a fully coupled THM model for fluid and
heat flow in discrete fracture networks and use the model to
gain insight into the flow channeling phenomenon associ-
ated with thermal drawdown. Despite the decades of effort
since the Fenton Hill experiment, EGS research is still in
the concept-validation phase and only a small number of
experimental sites have been developed so far (see reviews
in Jung 2013; McClure and Horne 2014). The objective of
the current study is to reveal physical mechanisms gov-
erning the flow-channeling process through the study of a
set of reasonable synthetic reservoir configurations, and to
provide practically useful guidance for the development
and operation of EGS. We focus on behavior of hot-wet-
rock (HWR) geothermal systems (Willis-Richards et al.
1996), where the natural fracture network provides the
majority of the permeability and the reservoir is saturated
with water in its natural state.
2 Coupled THM Model
2.1 Modeling Strategy
Our strategy for modeling coupled THM processes in the
production phase of EGS reservoirs is based on the fol-
lowing considerations and assumptions:
Matrix permeability of the rock formation is ignored
and all fluid flow is through the discrete fracture
network.
Fluid pressure is lower than the ‘‘jacking’’ pressure,
namely the minimum in situ principal stress (effective
stress, compression is positive) in the rock formation.
In this pressure regime, the change of fluid pressure in
fractures only induces minimal change of the stress
state in the surrounding rock matrix (Fu et al. 2012).
Therefore, the interaction between neighboring frac-
tures through a ‘‘stress shadowing’’ effect (Kresse et al.
2013) is insignificant and ignored in our model.
Because fractures in this pressure regime are still
closed, we consider the solid phase in the reservoir as a
continuum for the calculation of thermal stress.
Thermal drawdown in EGS reservoirs is a relatively
slow process. Field observation and numerical model-
ing have both indicated that its effect on reservoir
behavior is only noticeable over a time scale of months
(Bruel 2002). We assume that the flow field is in a
steady state within each time step. We use a time step
that is sufficiently small so that the simulation results
are insensitive to further reduction of the time step size.
The simulations are performed in two-dimensional
(2D) space under plane-strain conditions. The 2D
model can be considered as a horizontal cut through a
rock body containing steeply dipping fractures in the
normal stress regime (i.e. vertical stress is the major
principal component). Although it is well recognized
that many characteristics of random fracture networks
cannot be adequately represented by 2D models, and
the quantitative values from 2D models should not be
directly used for real world projects, we can still use 2D
models to gain insight into the physical processes
governing EGS reservoir performance, which would be
very useful for optimizing stimulation and production
strategies. Results of 2D models also inspire the
development of more sophisticated 3D models (Fu
et al. 2013; Settgast et al. 2012).
The numerical model consists of four main modules as
illustrated in Fig. 2. We briefly describe the framework of
the numerical method and discuss the coupling strategy
between different modules. The details of each module are
provided in subsequent sections.
In each time step, a rock joint model and a DFN-based
fluid flow solver are first invoked iteratively to calculate the
steady-state flow field in the fracture network. In this paper,
the word ‘‘joint’’ is used as a generic term referring to any
uncemented discontinuity in rock formations in a similar
fashion to Cook (1992). In each iteration, the flow solver
determines the pressure distribution within the fracture
network for the given aperture width distribution and
boundary conditions. The rock joint model then returns the
aperture width of each flow element for the next iteration,
determined by a function of the local total stress, the fluid
pressure provided by the flow solver, and the intrinsic joint
characteristics at each fracture segment. Once these itera-
tions converge, we obtain a fracture transmissivity field and
a flow field that are consistent with the given stress
boundary conditions, flow boundary conditions, and rock
joint characteristics for the current time step. Figure 3a
shows a random DFN and Fig. 3b shows the flow rate field
near the injection well solved by the DFN model where the
direction and width of the black triangles denote the flow
direction and flow rate, respectively.
Next, we use a porous medium-based heat and flow
transport model (i.e. a TH flow model) to advance the
temperature field for the present time step. To this end, we
Fig. 2 Main modules of the coupled THM model. Symbols t,Dt, and
Tdenote time, time increment, and temperature, respectively
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1003
123
map the DFN-based transmissivity field onto the perme-
ability field of a regular grid used by the porous medium
model. The fluid flow solution obtained by the TH flow
model is equivalent to that obtained by the DFN flow
solver. The flow solution is used to calculate the heat
transfer between the solid phase and the fluid phase, as well
as the convective heat transport along the fratures. At the
end of the time step, the reservoir temperature field is
obtained from the TH flow model, and mapped onto a finite
element method (FEM) solid mesh for calculation of the
thermal stress. Finally, we update the total stress on each
fracture segment used in the DFN flow module and start the
next time step. The time increment for a whole cycle
shown in Fig. 2is 4 months for all the simulations pre-
sented. We found that further reducing cycle duration did
not significantly alter the simulation results. Note that each
cycle involves many (typically hundreds of) time steps of
the porous medium solver.
2.2 DFN Flow Solver
The DFN flow solver uses a simple FEM formulation based
on two-node line elements. In two-dimensional space,
discrete fractures are geometrically represented by line
segments, and each fracture is discretized into line ele-
ments of approximately equal lengths. Intersection points
between fractures have to be represented by nodes, which
imposes an additional constraint on the discretization of the
fractures. According to the parallel plate laminar flow
assumption, the flow rate through a flow element between
node iand node jis
Qij ¼ðPiPjÞw3
12lijlF
ð1Þ
where P
i
and P
j
are the fluid pressure at two adjacent
nodes; l
ij
is the length of the element; l
F
is the dynamic
viscosity of the fluid; and wis the aperture width, which
Fig. 3 The mapping of variables used by different modules of the
coupled model. aA random discrete fracture network. bThe flow
field near the injection well in the DFN model after 3 years of
injection. cThe regular Cartesian grid used by the porous medium
model overlaid on the DFN. The DFN elements are shown in thin blue
lines. The darkness (gray to black) of the thickened cell–cell interface
lines quantifies the transmissivity between adjacent cells, with darker
color denoting greater transmissivity. dPressure field in the Cartesian
grid solved by the porous medium model. High pressure cells are
shown in red and unpressurized solid medium is in yellow.eThe
temperature field (red denotes high temperature and blue low
temperature) solved by the porous medium model. fThe thermal
stress (yy component; tensile stress in red color and compressive in
blue) field solved by the solid finite element model. These figures only
conceptually illustrate the mapping of variables between
meshes/models, so the color tables are not provided (color figure
online)
1004 P. Fu et al.
123
will be discussed in Sect. 2.3. A global system of gov-
erning equations is established by enforcing the mass
conservation condition that the net flow into each node is
balanced by the net flow out.
2.3 Rock Joint Model
The closure behavior of a fracture, namely the variation of
the aperture width wwith respect to the effective stress r0
is often characterized by joint models in rock mechanics, of
which the Barton-Bandis model (Bandis et al. 1983; Barton
et al. 1985) is a classical example. The model states
r0¼wmax w
aJbJðwmax wÞ;ð2Þ
where r0is the effective compressive stress, i.e. the dif-
ference between the total normal stress r
n
acting on the
fracture and the fluid pressure Pwithin the fracture; w
max
is
the aperture width at the zero-effective stress state, which
is essentially the maximum joint closure in the original
joint model of Bandis et al. (1983); a
J
and b
J
are two
material- and state-specific constants. This constitutive
model for rock joints has been widely used in various
numerical models for fracture-dominated geothermal
reservoirs (Kohl et al. 1995; Bower and Zyvoloski 1997;
Bruel 2002). If we identify a second reference state with
effective normal stress r0
ref
and the corresponding aperture
width w
ref
, the two material constants can be calculated as
aJ¼wmax
wmax wref
rref wref
and bJ¼wmax
wmax wref
rref wref
:ð3Þ
In our previous work (Fu and Carrigan 2012), we have
proposed to use parameters a
J
and b
J
as state variables to
reflect the effects of shear dilation on closure behavior of
rock joint. Since we focus on the production phase instead
of the stimulation phase of the reservoir, the two state
variables are constants for all fracture elements in the
current study. Note that the aperture width of individual
fracture segments can still vary based on the total stress and
fluid pressure.
2.4 Modeling Heat Transfer Using an Effective
Porous Medium Model
Heat transfer in the fractured reservoir is simulated using a
dual-continuum model implemented in a porous medium-
based flow and transport code NUFT (Nonisothermal
Unsaturated–saturated Flow and Transport). NUFT is
based on Darcy’s flow approximation and models multi-
phase, multi-component heat and mass flow and reactive
transport in unsaturated and saturated porous medium
(Nitao 1998; Hao et al. 2012). The formulation and veri-
fication of the dual-continuum model have been detailed in
Hao et al. (2013) and are not repeated here. In this section,
we present the procedure of converting the flow field
obtained by the DFN-based model to that on a regular
Cartesian grid used by NUFT.
Because the heat flow in fractured geothermal reser-
voirs is closely associated with fluid flow in the medium,
we have to create a flow field that is consistent with that
obtained by the DFN-based solver and compatible with the
regular Cartesian grid usedbyNUFT.Wedevelopeda
method similar to the ‘‘fracture continuum’’ method pro-
posed by Botros et al. (2008) and Reeves et al. (2008)and
overlay the DFN-based fracture elements onto the Carte-
sian grid used by NUFT as shown in Fig. 3c. In NUFT, the
permeability field is represented by the conductivity
between any two adjacent cells. In the two overlaid
meshes, if a fracture element geometrically intersects the
interface (a line segment in 2D) between two adjacent
porous medium cells in the regular grid, this fracture
segment’s contribution to the conductivity between these
two cells is
Dk¼ChðÞw3
12Að4Þ
where kis the permeability of the porous medium
according to Darcy’s law; Ais the area (length in 2D) of
the interface between the two cells; his the angle between
the fracture element and the Cartesian grid axis; and
C(h)=|sinh|?|cosh|, is a correction factor to compensate
for the longer flow paths in the Cartesian grid than the
corresponding length of the fracture. This mapping is
illustrated in Fig. 3c, where the darkness of the thickened
cell–cell interface lines denotes the transmissivity between
these two cells. The permeability of an inter-cell interface
can be contributed to by multiple fractures and the prin-
ciple of superposition applies. Only the fracture elements
that carry non-zero flow are included in the mapping, and
that is why most of the cell–cell interface lines are not
thickened, even though many of them are intersected by
fractures that do not carry flow. This is an advantage of our
proposed method compared to the fracture continuum
method (Botros et al. 2008; Reeves et al. 2008) in which a
similar mapping is carried out. In the latter the DFN are
pure geometrical entities and the flow field is only solved
by the porous medium solver. If the Cartesian grid spacing
is comparable to or greater than discrete fracture spacing,
false transmissivity can be generated by discrete fracture
segments that do not carry flow, a well known phenomenon
that causes over-prediction of flow (Botros et al. 2008;
Reeves et al. 2008). By ignoring DFN elements that do not
carry flow, our method maps the actual ‘‘flow field’’ solved
by the DFN solver instead of mere DFN geometries.
Therefore, the flow field solved by the porous medium
solver is nearly identical to the DFN flow field and the
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1005
123
results are insensitive to the resolution of the Cartesian
grid.
To continue the example illustrated by Fig. 3a–c,
Fig. 3d shows the pressure field solved by the porous
medium solver and Fig. 3e shows the temperature field
evolved by NUFT. Additionally, an example of a DFN-
based flow field and its equivalent representation with a
regular grid is presented in Fig. 13 along with the
numerical examples in Sect. 4.2.
2.5 Calculation of the Thermal Stress
As discussed in Sect. 2.1, we treat the rock body containing
closed fractures as a continuum for the calculation of
thermal stress. The finite element mesh for this purpose can
be established independently. We map the temperature
field onto the continuum FEM mesh at the center of each
element. The thermal stress field is calculated following the
procedure outlined in Sect. 2.10 of Cook et al. (2001). The
approach is a standard method employed in thermo-me-
chanical finite element analysis and not repeated here. The
thermal stress (yy-component) corresponding to the tem-
perature field in Fig. 3e is shown in Fig. 3f.
Initially, the fluid pressure is lower than the minimum
principal in situ stress, ensuring that all fractures are
closed. Over time, however, changes in the thermal stress
can reduce the total stress in the rock to the extent that
some fractures open due to the contraction of surrounding
rock. In this situation, the aperture size cannot be deter-
mined by the joint model in Sect. 2.3 and ideally should be
calculated with a fully coupled model, such as that of Fu
et al. (2013), with open fractures explicitly meshed in the
FEM model. For all of the simulations in the present paper,
this condition only occurs within a limited area near the
injection well. When these fractures (usually a small
number) open, the flow rate is determined by the closed
fractures that are connected to these open fractures, and
thus the transmissivity of the open fractures has minimal
effect on the overall flow field. Therefore, we assign a large
value, for instance 2w
max
to the aperture width of opened
fractures.
The three main modules in the numerical model use
three distinct meshes: the DFN solver uses an FEM mesh
composed of two-node line elements; NUFT uses a regular
Cartesian grid; and the thermal stress module uses a solid
mechanics FEM mesh. The three meshes do not need to
conform with each other as long as variable mapping
between meshes is correctly handled. In all the simulations
presented, the minimum distance between any two sub-
parallel fractures is 10 m, and the resolutions for the DFN
models, NUFT models, and the thermal stress FEM models
are all approximately 8 m, unless explicitly specified
otherwise.
3 A Highly Idealized Baseline Case
In this section, we study a reservoir with a highly idealized
fracture system as the baseline case, which enables us to
identify expected common behavior of fractured geother-
mal reservoirs, as well as a new mechanism that counter-
acting the flow channeling mechanism described in Sect. 1.
3.1 Model Setup
The idealized reservoir consists of two orthogonal fractures
sets forming a regular grid as shown in Fig. 4.A2D
coordinate system is established so that the x-axis points
east and the y-axis points north. We term the fracture set
parallel to the x-axis the ‘‘x-set’’ and the other the ‘‘y-set’’.
The domain, as well as the fracture network, is assumed to
be infinite, and the numerical model is made large enough
to minimize the effects of far-field boundaries. Fracture
spacing for both sets is 20 m. The in situ stress components
are r
x
=r
h
=18 MPa and r
y
=r
H
=25 MPa, where r
h
and r
H
are the minimum and maximum horizontal princi-
pal stresses, respectively. Note that r
x
happens to be the
normal stress acting on the y-set and r
y
acts on the x-set.
The production well is 600 m north of the injection well,
and each well is at an intersection of two fractures. The
original natural fluid pressure in the fracture system is
15 MPa, and the pressure boundary condition at the far-
field boundary is fixed at this value. The resolution of the
Fig. 4 Layout of the idealized reservoir consisting of two infinite
orthogonal fracture sets. Note that only the center portion of the
numerical model is shown. In all the layout maps in the present paper,
the locations of the injection well and the production well are denoted
by small circles
1006 P. Fu et al.
123
DFN mesh is 4 m. Some other important parameters are
shown in Table 1. Note that properties of real water are
functions of the water’s state such as temperature and
pressure. Using constant properties introduces certain
amount of error in the calculated results, mainly in calcu-
lated the pressure loss. However, since the main phe-
nomenon investigated by the current study, namely flow
channeling associated with reservoir temperature drop, is
caused by thermal–mechanical coupling that is indepen-
dent of water property change, these constant properties are
not expected to affect the comparison between the sce-
narios investigated herein.
Although we use the same rock joint parameters for the
two joint sets, their initial apertures are affected by the
anisotropic in situ stress and thus not the same. According
to the joint model described by Eq. (2), the aperture widths
for the x-set and y-set with zero-fluid pressure are 0.066
and 0.082 mm, respectively. The y-set has significantly
higher hydraulic transmissivity than the x-set, which is the
primary reason for the north–south well layout. We term
the y-set fractures the primary set and the x-set the sec-
ondary set.
3.2 Pumping Pressure—Circulation Rate Response
of Reservoir Before Thermal Drawdown
For all the simulations in the present paper, we use flow
rate–controlled boundary conditions at the two wells. The
injection rate is fixed at the same value as the production
rate, emulating a common circulating strategy used in
existing EGS sites (Genter et al. 2012,2013; Hogarth and
Bour 2015). To determine an appropriate flow rate, we run
a series of simulations at different circulation rates and
obtain the injection and extraction pressure required as
shown in Fig. 5. Note that all pressures presented in the
current paper are the pressure at the reservoir depth. The
results indicate that a higher circulation rate would require
higher injection pressure and lower extraction pressure
(higher net extraction pressure or stronger ‘‘suction’’), as
expected. Both curves are nonlinear, especially the
extraction curve, which reflects the fact that as we increase
the net extraction pressure (the absolute difference between
the extraction pressure and the far-field pore pressure) the
aperture near the extraction well decreases and the system
hydraulic impedance increases. This implies that with
increased pressure significantly more pumping power is
required for the same amount of marginal increase of cir-
culation rate. Based on the results, we choose 20 liters per
second per 100 m thick reservoir (L/s/100 m) as the cir-
culation rate at an initial injection pressure of 16.5 MPa
and an initial extraction pressure of 9.7 MPa for the anal-
ysis in the rest of Sect. 3. Since 9.7 MPa is the hydrostatic
pressure at approximately 1 km depth, a downhole pump
would be required if the reservoir is deeper than 1 km.
3.3 Reservoir Behavior Without
Thermo-Mechanical Effects
Figure 6shows the flow field obtained by the DFN solver
at the beginning of the production phase (i.e. no significant
temperature change in the reservoir has occurred). In this
figure and all subsequent figures quantifying DFN flow
fields, we use the orientation and width of the gray trian-
gles to denote the flow direction and flow rate, respectively.
Assuming 100 m thick reservoir, a fracture flow rate of
1.0 L/s is corresponding to a triangle 2.4 m wide. The scale
of flow visualization, i.e. the ratio of triangle width to
fracture flow rate is the same for all plots in the current
Table 1 Model parameters for
the idealized baseline
simulation
Parameter Value
Original in situ stress r
x
=r
h
=18 MPa (east–west)
r
y
=r
H
=25 MPa (north–south)
Original pore pressure P
0
=15 MPa
Rock joint parameters w
max
=1.0 mm
r
ref
=20 MPa
w
ref
=0.08 mm
Initial reservoir temperature T
0
=150 C
Injection fluid temperature T
i
=50 C
Mechanical properties of rock Young’s modulus E=20 GPa
Poisson’s ratio m=0.2
Linear thermal expansion coefficient a
L
=8910
-6
Thermal properties of rock Thermal conductivity K
r
=3 W/m/C
Heat capacity C
r
=2.5 MJ/m
3
/C
Fluid properties Dynamic viscosity l
f
=0.001 Pa s
Heat capacity C
f
=4.2 MJ/m
3
/C
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1007
123
paper. A few y-set fractures near the center of the domain
carry the majority of the flow. In this region, the flow rate
in the y-set fractures is substantially higher than in the x-set
fractures, because the total stress on y-set is lower than that
on x-set, resulting in wider apertures. However, because
only one fracture in the y-set is directly connected to the
two wells, flow in all the other y-set fractures must be
‘fed’’ by x-set fractures intersecting with them. Therefore,
the low conductivity of the x-set fractures is the main
reason why more dispersed flow patterns cannot form
under the given conditions. We term the flow along the
y-direction the primary flow and that along the x-direction
the secondary flow. Clearly, flow in both directions is
needed to form a flow network. Also note that there is a
significant amount of fluid injected into the reservoir flows
along the negative y-direction, i.e. the direction away from
the production well. Figure 6b shows that such ‘‘runaway’
flow is gradually diverted by x-set fractures, and it even-
tually reaches the production well through peripheral flow
channels. The flow into the production well that originates
from the far-field (as shown in Fig. 6c) is caused by the
same mechanism. In this paper, we refer to such flow as
‘peripheral flow’’. The aforementioned behaviors of the
flow network are clearly illustrated by Fig. 7, where flow
diversion and merging have caused discontinuity in the
flow rate along the two fractures shown, at x=0 and
x=60 m, respectively.
If we disregard the thermo-mechanical (TM) effects on
flow channeling, we can directly use NUFT to simulate the
temperature field evolution in the reservoir without
requiring the full procedure shown in Fig. 2. The results
provide a useful baseline reference for the study of flow
pattern changes due to TM effects. The evolution of pro-
duction temperature for this scenario is shown in Fig. 8as a
solid line, and the reservoir temperature fields 5, 10, 20,
and 30 years into the production phase are shown in Fig. 9.
According to the simulation results, the cooling front
arrives at the production well in less than 5 years of pro-
duction. The production temperature gradually decreases
afterwards and is approximately 98 C after 30 years of
production.
Fig. 5 Pumping pressure—circulation rate relationship of the ideal-
ized reservoir. The unit of circulation rate is liter per second for a
100 m thick reservoir. The pressure is that at the intersection between
the wellbores and the reservoir
Fig. 6 Initial flow field in the idealized reservoir. The direction and
width of the gray triangles denote the flow direction and flow rate,
respectively. Assuming 100 m thick reservoir, a fracture flow rate of
1.0 L/s is corresponding to a triangle 2.4 m wide. This ratio applies to
all flow rate visualizations throughout the paper wherever applicable.
The simulation domain is 1600 m 91600 m and not fully shown.
Fractures with flow rates smaller than 0.2 L/s are not shown. aThe
domain enclosing the two wells; bmagnifies the region around the
injection well; and cmagnifies the region around the production well
1008 P. Fu et al.
123
3.4 Coupled THM Simulation Results
If we invoke the THM coupling loop shown in Fig. 2, the
flow pattern will evolve with the temperature field. The
production temperature history obtained by the coupled
simulation is shown as the dotted line in Fig. 8. Snapshots
of the temperature and flow fields are shown in Fig. 10.
By comparing the temperature and flow fields between
Figs. 9and 10 at year 5, we see that the TM effects tend to
divert flow from the center fracture in the y-set, which
directly connects the two wells, to a few y-set fractures
running parallel to the center fracture. This causes a
slightly more diffuse flow pattern. This phenomenon is also
evident in Fig. 7: after 5 years, the flow rate in the fracture
at x=0 m between y=-300 m and y=-200 m is
substantially lower than the initial state; and in the fracture
at x=60 m flow rate has significantly increased in the first
5 years. This trend is also consistent with the observed
response of the temperature field: when the TM effects are
considered, the cooled zone is wider and the cooling front’s
propagation toward the projection well is slightly slower.
The TM effects substantially impede peripheral flow
(defined in Sect. 3.3) in the reservoir. After 20 years, flow
is almost completely concentrated in the cooled rock vol-
ume. This is one of the factors contributing to the fast
decrease of production temperature after thermal break-
through. In the scenario ignoring TM coupling, nearly half
of the flow into the production well is through peripheral
flow channels, and this portion of the fluid is not affected
by the cooling of the interior reservoir. Therefore, the fluid
extracted from the production well is indeed a mix of the
relatively cold fluid from the interior flow and the hot fluid
from the peripheral flow. On the other hand, because TM
coupling impedes peripheral flow, the flow into the pro-
duction well is primarily through the cooled reservoir, so
the production temperature declines rather rapidly. Due to
the same mechanism, the cooled zone extends quite far in
the negative y-direction if TM coupling is ignored, while
this extension is impeded when the full TM coupling is
considered.
3.5 Anisotropic Thermal Stress and its Implication
for Flow Channeling
We observe in Figs. 9and 10 that the cooled zone in the
reservoir elongates along the primary flow direction
because of the fast cooling of rock adjacent to the fractures
that carry high flow rate. Understanding of the anisotropy
in thermal stress caused by this elongated cooling geometry
is critical for gaining insight into the TM effects on flow
channeling. To this end, we consider an idealized case for
which closed-form solutions for thermal stress are avail-
able. This infinite 2D medium (plane-strain) has homoge-
neous physical and mechanical properties except that the
temperature of an elliptical zone is DTlower than that of
the rest of the medium, as illustrated in Fig. 11. The two
principal axes of the ellipse align with the two coordinate
axes, respectively, and the dimensions are 2aalong the
x-direction and 2balong the y-direction. Thermal stress
develops in this cooled zone as well as in the medium
surrounding it as a result of the cooling. The thermal stress
inside the cooled zone is homogeneous, which can be
calculated using our finite element model and can also be
calculated using the following equations, which are
Fig. 7 Flow rate along two y-set fractures, one at ax=0 and the
other one at, bx=60 m as marked in Fig. 5. The injection well is
located at x=0, y=-300 m and the production well at y=300 m.
Flow along the positive direction of the y-axis is considered to have a
positive flow rate and against this direction negative. Flow rate along
each straight fracture is continuous within each 20 m segment
between intersections but appears discontinuous due to the diversion
of flow to or from the x-set fractures
Fig. 8 Evolution of fluid temperature at the production well for the
idealized reservoir
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1009
123
simplified forms of the solution provided by Mindlin and
Cooper (1950):
rT
x¼aEDTaL
ðaþbÞð1mÞ;ð5Þ
rT
y¼bEDTaL
ðaþbÞð1mÞ;ð6Þ
where Eis the Young’s modulus of the medium; mis the
Poisson’s ratio of the medium; and a
L
is the linear thermal
expansion coefficient. Both normal components are tensile,
which result in the negative sign. The ratio of the magni-
tude of the two thermal stress components rT
x.rT
y

happens to be the aspect ratio of the ellipse. Note that
closed-form solutions for thermal stress are only available
for such a highly idealized case. Thermal stress for all the
cases in the current paper is calculated using coupled
thermal–mechanical finite element analysis.
Although the shape of the cooled zones shown in Figs. 9
and 10 is not exactly elliptical and the temperature in the
cooled zone is not uniformly distributed, the anisotropy in
thermal stress, shown in Fig. 12, resembles that of the
elliptical cooled zone scenario to some extent. Therefore,
the thermal stress along the primary flow direction (i.e.
y-direction) is substantially greater (in absolute magnitude)
than that along the secondary flow direction. Since thermal
stress in the cooled zone is tensile and it tends to reduce the
total normal stress (compressive) on fractures, the aniso-
tropic thermal stress opens the secondary fracture set (the
x-set) more than it does the primary set. As discussed in
Sect. 3.3, this results in a more diffuse flow pattern, and
thus flow must be fed into more primary set fractures
through secondary set fractures. However, under aniso-
tropic in situ stress, the secondary set acts as a bottleneck in
the system and prevents highly diffuse flow patterns from
forming. The anisotropic thermal stress is likely to
Fig. 9 Reservoir temperature
distribution in the idealized
reservoir if thermo-mechanical
effects are ignored. The flow
field is overlaid onto the
temperature field but it does not
evolve over time since the THM
coupling is disabled
Fig. 10 Reservoir temperature
distribution in the idealized
reservoir if thermo-mechanical
coupling is engaged. The flow
field is overlaid onto the
temperature field and evolves
over time along with the
temperature field evolution
1010 P. Fu et al.
123
counteract the anisotropic in situ stress and enhance the
conductivity of the secondary set fractures. This is the main
reason for the more diffuse flow pattern and wider cooled
zone in Fig. 10 than those in Fig. 9.
In Fig. 12 we also observe significant compressive
thermal stress (denoted by the blue regions) develops along
the periphery of the reservoir. This compressive stress
increment tends to further compress the fractures around
the cooled reservoir, which is an important mechanism that
impedes peripheral flow.
In summary, the analysis of the highly idealized reser-
voir reveals the primary effect of TM coupling: it causes
more open fractures inside the cooled reservoir and tighter
fractures in the exterior compared with the initial states.
The combined effect is that flow tends channelize inside
the cooled reservoir, inducing rapid temperature decreases
once thermal breakthrough has taken place. As a secondary
effect, the anisotropy in the thermal stress increment tends
to open the secondary set more than it does the primary set,
which encourages a more diffuse flow pattern well before
thermal breakthrough takes place, at least for fracture
networks with intensive interconnectivity. This effect can
delay thermal breakthrough.
4 Behavior of Random Fracture Networks
In this section, we investigate the THM responses of
reservoirs with various fracture network patterns and well
spacing. In real world reservoirs, natural fractures were
created by a variety of geophysical and geological pro-
cesses in rock formations. Certain characteristics of the
natural fracture system in a given formation can be quan-
tified, at least to some extent, through observations on
formation outcrops and wellbore logs (e.g. Engelder et al.
2009), but such knowledge is generally scarce. Therefore,
we investigate a number of artificially generated fracture
networks that collectively represent a variety of distinct
characteristics of fracture networks. The main objective is
to reveal how these network characteristics qualitatively
affect the thermo-mechanical-hydrological behavior of the
reservoir, rather than to quantify the performance of
specific reservoirs.
4.1 Reservoir Characteristics
We first investigate five distinct fracture networks, Net-
works B through F, illustrated in Fig. 13. Network A
denotes the idealized case introduced in Sect. 3.
A few properties are shared by all of the fracture net-
works. All networks have the same fracture intensity in
terms of total fracture trace length (area in 3D) per unit
area (volume in 3D). The initial pore pressure, temperature,
and in situ stress of all the reservoirs are the same as those
of the baseline case. We also use the same circulation rate,
20 L/s/100 m thick reservoir for all the cases.
Geometrical characteristics of a fracture network in 3D
are usually statistically quantified by a rather complex set
of parameters (Dershowitz and Einstein 1988). In 2D, the
situation is simpler and the main difference between 2D
fracture networks is the fracture pattern, namely orientation
and length distributions. In Network B, the orientations of
fractures follow a uniform distribution within all possible
directions, and the concept of ‘‘fracture sets’’ does not
apply to this network. If we use a variable hto denote the
orientation of a fracture with respect to the x-axis, hfol-
lows a continuous uniform distribution in the interval
Fig. 11 Geometry of an elliptical-shaped cooling zone in an infinite
medium. The analytical solution for the thermal stress in the cooling
zone demonstrates the relationship between the shape of the cooling
zone and the anisotropy of the thermal stress
Fig. 12 Thermal stress in the idealized reservoir after 20 years of
production. Compressive stress increment is positive
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1011
123
0Bh\180. Networks C through F each have two
distinct fracture sets. We term the set that is approximately
along the north–south direction the ‘‘primary set’’ and the
other the ‘‘secondary set’’, denoted by subscripts ‘‘P’’ and
‘S’’, respectively. The orientations and lengths (l) of each
fracture are randomly generated within a specified range.
These ranges are provided in Table 2for all the networks.
Note that the fracture generation algorithm enforces the
rule that no sub-parallel fractures should intersect with
each other. The two sets in Network C have similar fracture
lengths. The primary set in Network D has significantly
longer fracture than the secondary set, whereas fractures in
the secondary set of Network E are significantly longer
than those in the primary set. The two sets in Network F
have similar fracture lengths, but the fractures are much
shorter than those in Network C.
Although all networks have the same fracture intensity,
the permeability provided by each network also depends of
the connectivity of the fractures, which, to some extent, can
be quantified by the average number of fracture–fracture
intersections (n
i
) on each fracture. The n
i
values for all the
networks are shown in Table 2. Networks B through E are
all well above the percolation threshold (Berkowitz and
Ewing 1998), which means that many flow paths can be
established within the fracture network between two given
points. On the other hand, Network F is barely above the
percolation threshold. In order to carry out a ‘‘fair com-
parison’’, it is highly desirable to study and compare
reservoirs under the same production rate, which requires
comparable overall hydraulic impedances. Among other
parameters, fracture intensity, fracture orientations, frac-
ture dimension, fracture connectivity, and in situ joint
characteristics directly affect the hydraulic impedance of
the reservoirs. We choose to alter the joint parameters of
these networks to compensate for the difference in fracture
connectivity so that the overall flow impedances are com-
parable across all scenarios with the same fracture inten-
sity. The current study focuses on reservoir behavior
common to all the scenarios evaluated and none of the
conclusions to be drawn is a result of the specific joint
parameter values. We are primarily concerned with the
evolution of flow impedance of each individual scenario,
and do not intend to compare the absolute values of flow
impedance across different reservoirs. Therefore, the joint
parameters used for the different reservoir scenarios do not
affect the conclusions reached in this study. The approach
taken is analogous to a comparison of actual reservoirs
with different fracture connectivities but similar overall
hydraulic impedances.
For each network, excluding Network F, we evaluate
three inter-well distances: 400, 600, and 800 m. In the case
of Network F, only the 600 m inter-well distance is con-
sidered. The production well is due north of the injection
well. To establish a connection between the wells and the
in situ fracture network, we create a hydraulic fracture,
running 80 m to the north and to the south of each well. In
all other regards, we assume the hydraulic fractures to
behave in the same manner as the pre-existing natural
fractures. The simulation domain is 2400 m 92400 m in
size, sufficient for simulating the thermal, hydrological,
and mechanical effects of the far field. In Sects. 4.24.6,
we focus on the scenarios with 600 m inter-well distance
and study the effects of well distance in Sect. 4.7.
4.2 Initial Flow Field
The initial flow patterns for the five fracture networks with
600 m well spacing are shown in Fig. 14. The same
Fig. 13 Fracture connectivity patterns for the five representative fracture networks. Only the center portion of each network is shown. The
injection well and production well denoted are 600 m apart, although 400 and 800 m spacings are also investigated
1012 P. Fu et al.
123
circulation rate (20 L/s/100 m) is applied to all the net-
works. The initial pressure drop between injection and
production wells for Networks B to F is 7.0, 10.6, 8.3, 12.9,
and 10.6 MPa, respectively. As different joint parameters
are used for each network, the comparison of these values
does not offer much insight into hydraulic behaviors of
these networks.
In Network B, the fracture orientations are isotropic, so
the concepts of primary and secondary fracture sets are
inapplicable. For Network C, the primary set and the sec-
ondary set are geometrically similar. However, their aper-
tures are significantly different because the in situ stresses
in the x-direction (r
x
=18 MPa, acting on the y- or pri-
mary set fractures) and that in the y-direction (r
y
=25 -
MPa, acting on the x- or secondary set fractures) are rather
different. These two networks are similar to the baseline
regular Network A in the sense that the two fracture sets
cannot be differentiated based on geometrical features
only. Consequently, the initial flow patterns of these three
networks exhibit certain similarities: Flow tends to con-
centrate in fractures along the north–south direction. Some
secondary set fractures (east–west oriented fractures in
Network B) have to be engaged as they are necessary for
connecting the primary set fractures together. In Network
D, the primary-set fractures are longer than the secondary-
set fractures and on average each primary-set fracture
intersects 6.74 secondary-set fractures while each sec-
ondary fracture intersects 2.48 primary-set fractures. Flow
in a primary set fracture in Network D can travel a rela-
tively long distance without having to diverge into sec-
ondary set fractures. Meanwhile, flow in a secondary
fracture does not need to travel a long distance to flow into
another primary set fracture. Therefore, the active flow
paths in Network D do not spread as wide as those in
Network C in the east–west direction. The situation in
Network E is the opposite and consequently, the active
flow paths spread more widely in the east–west direction
than those in Networks C and D. Network F is a special
scenario with low fracture connectivity that is barely above
the percolation threshold. Apart from flow to and from the
far field, there is only one major flow path between the two
wells. Although this flow path splits at some points along
the way, the branches soon merge back into a single path.
All the five initial flow networks have significant peripheral
flow through the far field network.
4.3 Reservoir Performance Without TM Coupling
If we ignore the TM coupling for the sake of understanding
the impact of channelized flow, we can use NUFT alone to
calculate the responses of the reservoirs during heat pro-
duction. The production temperature evolution for all the
six fracture networks, including the regular grid discussed
in Sect. 3, is shown in Fig. 15. Note that simulations
ignoring TM coupling only have conceptual significance,
since TM coupling always takes place in a real reservoir.
However, we can use the results as a proxy for character-
izing the diffusivity of the initial flow network, and the
results are consistent with a visual assessment of Fig. 14:
flow paths in Network B and those in Network C have
comparable diffusivity, and these two reservoirs have
similar thermal performance; flow paths in Network D are
slightly more concentrated than those in Network C, and its
thermal performance is moderately worse; Network E has
the most diffuse flow paths among all the six scenarios and
it also has the longest lasting thermal performance. Net-
work A and Network F have similar thermal performance
that is significantly worse than that of the other four sce-
narios. Although they are at the two ends of the percolation
number (i.e. fracture connectivity) spectrum, they share
one common characteristic: the flow field is dominated by a
single flow path. For Network A, it is the fracture directly
connecting the two wells; for Network F, only one viable
flow path between the two wells can be established besides
peripheral flow paths. The flow path in Network A has
much lower hydraulic impedance that that in Network F,
Table 2 Characteristics of the five randomly generated fracture networks
Network B Network C Network D Network E Network F
Fracture orientation 0Bh\18075Bh
p
\85
-5Bh
s
\5
75Bh
p
\85
-5Bh
s
\5
75Bh
p
\85
-5Bh
s
\5
75Bh
p
\85
-5Bh
s
\5
Fracture length 150 m \l\300 m 150 m \l
p
\300 m
150 m \l
s
\300 m
150 m \l
p
\300 m
60 m \l
s
\120 m
60 m \l
p
\120 m
150 m \l
s
\300 m
60 m \l
p
\120 m
60 m \l
s
\120 m
Fracture connectivity n
i
=7.08 n
i_p
=6.38
n
i_s
=6.42
n
i_p
=6.75
n
i_s
=2.48
n
i_p
=2.50
n
i_s
=6.66
n
i_p
=2.63
n
i_s
=2.59
Joint model parameters w
max
=1.0 mm
r
ref
=20 MPa
w
ref
=0.12 mm
w
max
=1.0 mm
r
ref
=20 MPa
w
ref
=0.12 mm
w
max
=1.0 mm
r
ref
=20 MPa
w
ref
=0.15 mm
w
max
=1.0 mm
r
ref
=20 MPa
w
ref
=0.15 mm
w
max
=1.0 mm
r
ref
=20 MPa
w
ref
=0.3 mm
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1013
123
but this difference only affects the overall hydraulic
impedance of the reservoirs, not the thermal performance
without TM coupling.
The temperature distribution in the reservoirs after
20 years (TM effects ignored) of production is shown in
Fig. 16. The shapes of the cooled zones are consistent with
the flow fields: if the flow paths spread wide along the east–
west direction, the corresponding cooled zone is also wide.
The propagation of the cooling front is slower towards the
production well if the cooled zone is wider, implying more
desirable thermal performance. The cooled zones in all five
simulated reservoirs extend significantly southwards due to
the peripheral flow.
4.4 Reservoir Behavior With TM Coupling
The production temperature of the five random fracture
networks calculated by THM coupled simulations is shown
in Fig. 17 along with the results for Network A. The
temperature and flow fields after 2.5, 5, 10, 20, and
30 years of production at the constant circulation rate of
20 L/s are shown in Fig. 18. The injection well and pro-
duction well are 600 m apart in all the results of the current
section.
The most striking observation when we compare the
results in Fig. 17 with those in Fig. 15 is the rapid tem-
perature decline in all cases after thermal breakthrough. In
Fig. 18 we see that in each reservoir as the cooling front
propagates towards the production well, flow always con-
centrates in a small number of fractures in the cooled zone,
Fig. 14 Initial flow pattern in the five random fracture networks with
600 m well distance. Fractures with flow rate smaller than 0.2 L/s are
not shown. For Network B, flow patterns obtained by both the DFN
solver and NUFT are shown. In the NUFT result for Network B,
porous medium cells with higher flow rate are rendered darker
Fig. 15 Production temperature evolution without TM coupling for
the six fracture Networks (AF) with an inter-well separation distance
of 600 m
1014 P. Fu et al.
123
regardless of how dispersed the initial flow network had
been. The TM effect always impedes peripheral flow, in a
fashion similar to that demonstrated in Sect. 3, due to the
compressive hoop thermal stress around the cooled zone.
This effect further increases the severity of the flow
channeling.
Among all the fracture networks, Network E has the
most diffuse initial flow pattern, owing to the lack of direct
flow pathways connecting the two wells. As a result, the
thermal breakthrough in Network E takes place signifi-
cantly later than that in other networks. Nevertheless, flow
channeling into the cooled zone is inevitable. Because the
cooled zone does not extend straight between the two
wells, Network E has longer flow paths after thermal
breakthrough than those in the other networks. This results
in a more gradual production temperature decline than that
in the networks with shorter flow paths.
Network F is a special case with a low fracture con-
nectivity that is barely above the percolation threshold. The
TM coupling only has a moderate effect on the flow field in
this fracture network, because there is only one viable flow
path between the two wells in the interior of the reservoir.
The TM effects tend to decrease hydraulic impedance of
the interior portion of the reservoir and reduce peripheral
flow, but the change of overall flow pattern is much less
substantial than that for Networks B through E. Therefore,
thermal breakthrough takes place in Network F the earliest
among all networks, because the flow pattern is the least
diffuse, but the temperature decline is more gradual than
that of other networks, because a relatively long flow path
is retained between the two wells. The decline in
Fig. 16 Reservoir temperature field without TM coupling after 20 years of production. The initial flow fields are overlaid onto the temperature
field
60
80
100
120
140
160
0 5 10 15 20 25 30
Production temperature (°C)
Production time (year)
Network A
D
F
E
C
B
Fig. 17 Production temperature evolution with TM coupling for the
six fracture Networks (AF) with an inter-well separation distance of
600 m
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1015
123
Fig. 18 Temperature and flow fields of in the five random fracture networks during production. Inter-well distance is 600 m for all cases shown
1016 P. Fu et al.
123
production temperature from Network F is also relatively
gradual for a similar reason: the topological characteristics
of this reservoir do not allow for a short (and straight) flow
path to form between the two wells.
Geometrical and topological characteristics of the frac-
ture network have profound effects on thermal perfor-
mance of a reservoir. Note that all networks we studied so
far have the same fracture intensity. Fracture aperture
width mainly affects the reservoir hydraulic impedance
while its effects on flow field patterns are insignificant.
Therefore, the observed differences are mainly caused by
the differences in fracture geometry and topology. Gener-
ally speaking, networks with more diffuse initial flow
patterns (e.g. Network E) tend to have later thermal
breakthrough. However, the TM effects, which dictate the
flow pattern evolution during heat production, are highly
dependent on characteristics of the fracture network in a
rather complex way.
4.5 The Evolution of Overall Hydraulic Impedance
As reservoir temperature decreases, the overall hydraulic
impedance between the two wells is expected to decrease
owing to less compressive total stress, and thereby smaller
effective stress on the fractures. This phenomenon has been
observed in real world EGS reservoirs (Kohl et al. 1995).
Figure 19 shows the evolution of overall hydraulic impe-
dance of each reservoir with respect to production time,
where DPis the pressure difference between the two wells
and the subscript ‘‘0’’ denotes the initial state. By com-
paring Figs. 19 with 17 we conclude that the reduction of
hydraulic impedance is highly correlated with the decline
of production temperature, which is a proxy for overall
reservoir temperature. A special case is Network A where
the impedance first decreases and then moderately increa-
ses between year 1 and 7. This is believed to be caused by
the compressive thermal stress at the periphery of the
cooled zone, which tends to tighten the fractures. This
phenomenon is only observable on Network A but not the
other networks, likely due to the unique feature of Network
A that much of the permeability in the reservoir is provided
by the fracture directly connecting the two wells.
4.6 The Effects of Random Realizations
So far we only generated one random realization for each
set of fracture network characteristics. To evaluate whether
the results and conclusions are sensitive to random real-
izations, we generate five additional realizations for Net-
work B and simulate the fluid circulation and heat
production with THM coupling. Figure 20 shows the initial
flow field and the flow and temperature fields after 20 years
of heat production at 20 L/s/100 m thick reservoir for these
five random realizations. The evolution of production
temperature for these five realizations (‘‘Realization 1’’ to
‘Realization 5’’) along with that for the Network B real-
ization in Sect. 4.2 (‘‘Realization 0’’) is shown in Fig. 21.
Although the production temperature evolution curves
of the six realizations span a relatively wide range, the
variation does not call into question any of the observations
in Sect. 4.4 as summarized below.
1. All the six curves show rapid post-breakthrough
temperature decline.
2. The networks with more diffuse initial flow patterns
(e.g. Realizations 3 and 4) have later thermal break-
through than those with more concentrated initial flow
fields do.
3. Figure 21 compares the production temperature curves
of the six Network B realizations with those of
Network E and Network F. We argued in Sect. 4.4
that the heat production characteristics of Networks E
and F are rooted in their respective fracture network
features: Network E’s late breakthrough and gradual
post-breakthrough temperature decrease are caused by
the lack of direct short connections between the two
wells and the abundance of tortuous flow paths,
whereas Network F’s early breakthrough and relatively
slow post-breakthrough temperature decrease are the
results of the low percolation number. Although the six
realizations of Network B show a relatively wide range
of variation in heat production characteristics, they still
share many characteristics that are distinctly different
from those of Networks E and F. The thermal
breakthrough time of all the six Network B realizations
is later than that of Network F but earlier than that of
0
0.2
0.4
0.6
0.8
1
0 5 10 15 20 25 30
ΔPP0
Production time (year)
Network A
D
F
E
C
B
Fig. 19 Evolution of hydraulic impedance for the six simulated
reservoirs (AF) with a 600 m inter-well separation distance
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1017
123
Network E. Their post-breakthrough temperature
decrease is significantly faster than those of Networks
E and F. This proves that the different behaviors of the
networks discussed in Sect. 4.4 are indeed primarily
caused by the distinct statistical characteristics of the
networks, not merely reflecting the random nature of
the problem.
4.7 The Effects of Well Distance
Intuitively, increasing the well distance should increase the
extractable heat by enlarging the accessible reservoir vol-
ume while potentially requiring greater pumping effort. To
study these effects, we perform simulations with well dis-
tances of 400 and 800 m in addition to the 600 m well
distance simulations for Networks B, C, D, and E. One
stochastic realization is generated for each combination of
well distance and network characteristics, except that
multiple realizations of Networks B and E at well distances
of 600 and 800 m are included to evaluate the effects of the
random process that creates the fracture networks. The
injection-extraction pressure drop in the initial state for
different fracture networks is summarized in Fig. 22. Each
column of data point(s) represents a combination of well
distance and fracture network characteristics. Multiple data
points are shown for those combinations (Networks
B-600 m, B-800 m, E-600 m, and E-800 m) with a series
of stochastic realizations.
The effects of well distance on flow impedance do not
seem to be definitive. For the combinations with multiple
realizations, increasing the well distance seems to increase
the total impedance of the system, but the random variation
of the results is also very substantial. A closer inspection of
individual fracture network characteristics reveals that the
observed variation of flow impedance is heavily affected
Fig. 20 Five additional random realizations with statistical characteristics identical to Network B. The images in the upper row show the initial
flow field, and those in the lower row show the flow field and reservoir temperature field after 20 years of production
Fig. 21 Production temperature histories of six random fracture
network realizations with the same statistical characteristics as
Network B. The results of Networks E and F are also shown for
comparison
1018 P. Fu et al.
123
by the number of natural fractures intersecting the
hydraulic fractures connecting to the wells, particularly
those connecting to the production well. This factor is not
controlled in the randomly generated fracture networks.
To compare the thermal performances of different well
distances in a concise manner, we plot the production life
of each layout at production temperatures above 145 and
100 C in Fig. 23a and b, respectively. The flow field and
temperature field after 20 years of production are shown in
Fig. 24. Overall, the effects of well distance on thermal
performance of the reservoir are very significant. For
Networks B, C, and D, the percentage of production life
increase is greater than the percentage of the increase of
well distances. In other words, the production life of each
fracture network increases much more than 50 % when the
well distance increases from 400 to 600 m, and life
increases much more than 33 % when the well distance
increases from 600 to 800 m. The baseline realization of
Network E shown in Fig. 18 is an anomalous case, as the
layout of 800 m well distance has slightly worse thermal
performance than the layout with 600 m well distance. In
the 600 m layout, the fracture connectivity, especially that
near the injection well, dictates that flow paths connecting
the two wells in a relatively direct manner cannot form,
resulting in long flow paths. In contrast, the 800 m well
distance layout for Network E happens to produce less-
tortuous connections between the two wells. Although this
small anomaly does not affect the validity of the afore-
mentioned overall trend of the effects of well distance, it
reemphasizes the fact that in a random fracture network the
inter-fracture connectivity and fracture-well connectivity
play a remarkable role in determining behavior of the
reservoir.
4.8 The Effects of Fracture Intensity
The fracture intensity in all the above simulations is con-
stant (0.1 m fracture length per m
2
area in 2D) across all
the fracture networks generated. We investigate the effects
of increased fracture intensity in the current section. We
generate random fracture Network G with the same frac-
ture orientation and length distributions as those in Net-
work C while the fracture intensity has been increased by
67 %. We also generate Network H based on Network E in
a similar fashion. The injection well and production well
are 600 m apart for both cases. For a given fracture length
and orientation distribution, the inter-fracture connectivity
increases as fracture intensity increases. n
i_p
and n
i_s
are
10.47 and 10.57, respectively for Network G, and 4.11 and
11.03, respectively for Network H. The joint model
Fig. 22 Injection-extraction
pressure drop in the initial state
for different fracture networks
and various inter-well
separation distances
Fig. 23 Reservoir production life at temperature above 145 C and above 100 C for different fracture networks and inter-well separation
distances
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1019
123
parameters for Networks G and H are the same as those for
Networks C and E, respectively. At the same circulation
rate of 20 L/s, the initial pressure difference between the
injection well and the production well is 3.13 MPa for
Network G, and 2.91 MPa for Network H, much lower than
the values for their low fracture intensity counterparts,
which is a direct result of the lower per-fracture flow rate.
Figure 25 shows the initial flow network patterns for
these two reservoirs. When flow in Network G is compared
with Network C (shown in Fig. 14) and H compared with E
(shown in Fig. 14), an expected consequence of the
increased fracture intensity is that flow distributes into
more fractures with each fracture carrying a smaller flow
rate. However, the overall flow patterns of Networks G and
H resemble those of C and E, respectively. As explained in
Sect. 4.3, NUFT simulation results without TM effects can
be used as a proxy for the degree of flow path diffusivity.
With the TM effects disabled, the evolution of production
temperature for Networks G and H is shown in Fig. 26a,
compared with the results of their low fracture intensity
counterparts (TM also disabled). Networks G and H per-
form slightly worse than Networks C and E, respectively.
Fig. 24 Reservoir fracture flow field and reservoir temperature field for different fracture Networks (B, C, D, and E) and inter-well separation
distances (400, 600, and 800 m) after 20 years of production
1020 P. Fu et al.
123
This is caused by the high fracture intensity networks’
ability to form less-tortuous flow paths than the low frac-
ture intensity networks can. Nevertheless, the difference is
small.
The THM coupled simulation results are shown in
Figs. 26b and 27. The cooled zone of a high fracture
intensity reservoir tends to be more consolidated into the
core of the reservoir than its low fracture intensity coun-
terpart. The thermal performance of Network G is com-
parable to that of Network C. The difference of thermal
performance between Networks H and E is remarkable.
Recall that the good thermal performance of Network E is
mainly caused by the lack of flow pathways directly con-
necting the two wells, which is combined effect of network
features and the particular well locations. The higher
fracture intensity in Network H allows much more direct
(i.e. straight) flow paths to form.
5 Concluding Remarks and Practical Implications
The current study investigates the effects of thermo-me-
chanical (TM) coupling on the performance of geothermal
reservoirs in discrete fracture networks, with a particular
focus on the phenomenon of flow channeling. A series of
discoveries and observations have been made through a
systematic investigation.
In addition to confirming the well-known flow chan-
neling mechanism, where flow concentrates into a small
number of flow paths inside the cooled zone, our numerical
simulation reveals a new TM mechanism that counteracts
flow channeling to some extent. This secondary mechanism
is related to the anisotropy in thermal stress caused by the
typically elongated cooling zone. Although the effects of
the secondary mechanism are not strong enough to sig-
nificantly alter the fate of flow channeling, it is possibly an
Fig. 25 Initial flow patterns of
Networks G and H
Fig. 26 The evolution of production temperature for high fracture intensity scenarios for asimulations without TM effects and bwith TM
effects. The comparison with the low fracture intensity counterparts is included
Thermal Drawdown-Induced Flow Channeling in Fractured Geothermal Reservoirs 1021
123
important factor contributing to the temporarily more dif-
fuse flow pattern suggested by tracer tests after some time
of production at Fenton Hill (DuTeaux et al. 1996).
Flow channeling seems to be inevitable in all of the
fracture networks simulated with TM coupling, despite the
wide variety of network characteristics under considera-
tion. The effects of flow channeling on the pre-break-
through production life is modest. However, flow
channeling causes very rapid production temperature
decline after thermal breakthrough, thereby severely
undermining the economic value of a post-breakthrough
reservoir. One reason for the rapid post-breakthrough
temperature drop is that the TM effects cause tensile stress
increments inside the cooled zone and compressive hoop
stresses along the periphery of the cooled zone, which
dramatically impedes peripheral flow and eliminates fluid
flow’s access to the exterior hot rock body. We did not
consider spatial variation of fracture properties in the
paper, although in real reservoir fractures in some regions
could be tighter than those in other regions. However, the
phenomenon that fractures carrying higher flow rate cool
the surrounding rock faster and flow tends to concentrate
more in the cooled zone is universally true, because it is a
result of simple thermal–mechanical coupling.
The current study highlights the important role of frac-
ture connectivity in determining the general behavior and
thermal performance of a fractured reservoir. Intensively
inter-connected fractures offer low hydraulic impedance
and consequently low pumping cost, but also enable the
formation of direct flow paths between the two wells,
which is a negative factor for reservoir thermal perfor-
mance. As long as fractures in the network are well
interconnected, increasing or decreasing fracture intensity
has no significant and consistent effect on effective pro-
duction life, although it does significantly affect the overall
hydraulic impedance of the system. Although the available
analysis does not point to specific network characteristics
that ‘‘optimize’’ reservoir performance, the current study
does highlight the importance of gaining deeper knowledge
on this subject.
For a given fracture system, it appears that the only
apparent way to effectively prolong the effective produc-
tion life is to place the two wells further apart. It is inter-
esting to observe that the overall hydraulic impedance is
not sensitive to well distance changes, and the modest
effect of well distance is often overshadowed by the ran-
dom nature of fracture networks.
Finally, we acknowledge that it would be inappropriate
to directly use our 2D model to quantitatively predict
actual reservoir performance. 3D fracture geometries and
flow fields are necessarily more complex than those in 2D.
However, the flow channeling and accelerated production
Fig. 27 Temperature and flow fields of in the two random fracture Networks (G and H) with high fracture intensity during production. Inter-well
separation distance is 600 m in both cases
1022 P. Fu et al.
123
temperature decline phenomena revealed and investigated
in the current study are direct consequences of two simple
physical processes: (1) the aperture and transmissivity of
rock joints increases as effective stress decreases, and (2)
the cooling of a finite zone causes tensile thermal stress
within the cooled zone and compressive hoop thermal
stress in the surrounding medium. These two processes are
true for both 2D models and 3D reservoirs alike. Therefore,
we believe that the discoveries in the current paper apply,
at least qualitatively, to real world reservoirs.
Acknowledgments The authors gratefully acknowledge the
Geothermal Technologies Office of the US Department of Energy for
support of this work. Additional support was provided by the LLNL
LDRD project ‘‘Creating Optimal Fracture Networks’’ (#11-SI-006).
An anonymous editor of the journal provided valuable advice that
substantially improved the quality of this paper, for which the authors
are especially grateful. This work was performed under the auspices
of the US Department of Energy by Lawrence Livermore National
Laboratory under Contract DE-AC52-07NA27344. This paper is
LLNL report LLNL-JRNL-644453.
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