Gas injection is an effective method to enhance oil recovery of low-permeability and tight reservoirs, while the complicated fractures distributed in the formation have a noticeable effect on the performance of gas injection. In this study, three methods of gas injection were employed to conduct microfluidic experiments using micromodels simulating fractured reservoirs. The sweep efficiency and oil displacement efficiency of pores and throats, fractures, and the whole region were measured respectively to evaluate the oil displacement effects of the different gas injection methods. Moreover, the microscopic displacement process and the morphology of residual oil in porous media were analyzed to investigate the behavior of gas activated oil. The experimental results show that there are three stages of gas displacing oil: the oil in fractures was displaced first, then the oil in the pores and throats around the fracture was displaced, and finally the gas channeling occurred in fractures. Moreover, the sweep efficiency and oil displacement efficiency showed a tendency of increasing fast first and then reaching a steady state. Simultaneous injection of gas and water showed an optimal enhanced oil recovery effect among these three injection methods. Gas can invade deep throats, and those are difficult for water to sweep. However, the higher viscosity of water endowed it a smaller mobility than gas. And, the channeling in the two-phase mixing region was inhibited more obviously. The overall sweep efficiency and oil displacement efficiency increased about 18.4% and 13.4%, respectively.
Gas injection is an effective method to enhance oil recovery of low-permeability and tight reservoirs, while the complicated fractures distributed in the formation have a noticeable effect on the performance of gas injection. In this study, three methods of gas injection were employed to conduct microfluidic experiments using micromodels simulating fractured reservoirs. The sweep efficiency and oil displacement efficiency of pores and throats, fractures, and the whole region were measured respectively to evaluate the oil displacement effects of the different gas injection methods. Moreover, the microscopic displacement process and the morphology of residual oil in porous media were analyzed to investigate the behavior of gas activated oil. The experimental results show that there are three stages of gas displacing oil: the oil in fractures was displaced first, then the oil in the pores and throats around the fracture was displaced, and finally the gas channeling occurred in fractures. Moreover, the sweep efficiency and oil displacement efficiency showed a tendency of increasing fast first and then reaching a steady state. Simultaneous injection of gas and water showed an optimal enhanced oil recovery effect among these three injection methods. Gas can invade deep throats, and those are difficult for water to sweep. However, the higher viscosity of water endowed it a smaller mobility than gas. And, the channeling in the two-phase mixing region was inhibited more obviously. The overall sweep efficiency and oil displacement efficiency increased about 18.4% and 13.4%, respectively.
Low permeability and tight
reservoirs play a significant role in
the development of oil and gas reservoirs because of the huge reserves.[1−3] However, as a result of its small pores and throats, it is extremely
difficult to develop compared with conventional reservoirs.[4−6] With the huge demand of economic and industrial development, expanding
the scale of development and especially enhancing the development
of low permeability and tight oil reservoirs is one of the urgent
problems to be improved.[7,8] Fractures are ubiquitous
in the reservoirs, especially in tight formations, such as the BachHo
oilfield in Vietnam, the Yanling oilfield in China, the Baobab oilfield
in Chad, etc.[9−11] In tight reservoirs, it is difficult for water to
be injected as a result of smaller pore and throat size, which is
detrimental to efficient development.[12−14] Compared with water,
gas is easier to inject into a tight formation, making it a more suitable
solution than water in tight reservoirs.[15,16] Among gas flooding methods, N2 is impressively insoluble
in water and chemically stable compared with hydrocarbon gas and CO2. Additionally, N2 has a small compressibility
factor and is therefore not easily compressed. These characteristics
endow N2 with the ability to replenish the formation energy
and maintain the formation pressure. N2 flooding is considered
to be an effective method to enhance oil recovery. However, fractured
reservoirs are characterized by well-developed fractures, low matrix
permeability, and high heterogeneity.[17−19] In addition, with the
external and internal effects such as weathering for many years, the
development degree of matrix and fractures in different parts of the
reservoir from top to bottom is different, which further exacerbates
the complexity and development difficulty of natural fractured reservoirs.[20−23] During the development process, the injected fluid channeling is
prone to occur along fractures and high permeability areas, which
makes it difficult to sweep the oil and reduce the ultimate oil recovery.[24,25] Due to high heterogeneity and structure complexity in naturally
fractured reservoirs, the inhibition of gas channeling is challenging
despite the existence of giant oil reserves in fractured reservoirs.[26,27]Understanding gas flow behaviors in porous media is critical
to
exploring how to enhance oil recovery efficiently by gas flooding.
Conn et al.[28] investigated the flow behaviors
and the effect of foam on enhanced oil recovery by using a microfluidic
chip with a wide central fracture. They clearly observed differences
in the flow of gas through fractures, pores, and throats. Bai et al.[29] performed gas huff and puff experiments in fractured
cores to study the effect of gas on residual oil distribution at fractures
and areas with different permeability levels. It can be seen that
the oil was primarily produced from the fractures and macropores,
while the residual oil in the fractured cores was mainly distributed
in small and medium pores and throats. Chen et al.[30] analyzed the effect of flue gas flooding on tight fractured
reservoirs and the distribution of residual oil after gas flooding
by a low-field nuclear magnetic resonance (LFNMR) system. They found
that the existence of fractures in cores reduced the oil recovery
significantly compared with a fracture-free core, playing a negative
role in enhanced oil recovery of gas flooding in tight reservoirs.
Zhang et al.[31] prepared a bulk gel by wormlike
micelles generated from a CO2-responsive smart mobility
control system to mitigate serious gas channeling and low sweep efficiency
of CO2 gas flooding for enhanced oil recovery in ultralow
permeability reservoirs. The experimental results showed that the
fracture was blocked, and the CO2 gas was diverted to the
pores and throats to displace the residual oil. Although many scholars
have previously carried out studies on the oil displacement characteristics
of gas in fractured cores, almost all of them simulate the case of
single-fracture cores, and there are still no reports on the visual
study of the case of multiple fractures, pores, and throats at the
same time. In particular, there is no previous study on gas flooding
and gas–water coflooding in porous media with different development
degrees of pores, throats, and fractures.In this study, pore-scale
flow behaviors of gas and the enhanced
oil recovery method for gas injection of fractured reservoirs were
explored by using microscopic visual porous media. The novel micromodels
with pores and throats as well as a complex network of fractures were
designed and fabricated to intuitively observe the pore-scale flow
behaviors of gas. Moreover, this paper mainly discussed the effect
of oil displacement in three types of porous media with different
development degrees of pores, throats, and fractures by three gas
injection methods. The optimal gas injection method for the development
of fractured reservoirs was evaluated from macroscopic and microscopic
perspectives.
Experimental Section
Materials
The experimental oil was
offered by the Research Institute of Petroleum Exploration and Development
(Beijing, China), with a viscosity of 12.5 mPa·s at room temperature
(25 °C). Nitrogen gas (purity of >99.99%) was purchased from
Beijing Jinggao Gas Co., Ltd., China. Ethanol and petroleum ether
were used to wash the microfluidic chips and purchased from Shanghai
Titan Scientific Co., Ltd., China. Deionized water was prepared for
glass cleaning and oil displacement.
Methods
Design and Preparation of Microfluidic Chips
To clearly study the flow behaviors of gas in porous media simulating
formation with fractures, three microfluidic chips are designed and
fabricated, as shown in Figure a–c. The pores and throats of porous media are designed
with regular shape, in which the pores are regular hexagons of equal
size and the throats are narrow channels connecting vertexes of hexagons.
The fractures are rectangular channels with random distribution. The
size of the porous media area in the microfluidic chip is 50 mm ×
50 mm. In order to simulate formation with different degrees of fracture
development, the fracture sizes of the three kinds of micromodels
are 200–300 μm, 100–200 μm, and 50–100
μm, respectively, and the number of fractures decreases successively.
The throat sizes of these three types of micromodels are correspondingly
15–20 μm, 8–12 μm, and 4–6 μm,
respectively. To study the law of different injection methods, a micromodel
with two inlets and two outlets was designed and fabricated as shown
in Figure d. The morphology
and size of pores, throats, and fractures in this micromodel was the
same as that shown in Figure a.
Figure 1
Schematic diagrams of microfluidic chips with one inlet and one
outlet, representing formation with rich fractures (a), poor fractures
(b), and medium number fractures (c) and a microfluidic chip with
two inlets and two outlets (d), representing formation with rich fractures.
Schematic diagrams of microfluidic chips with one inlet and one
outlet, representing formation with rich fractures (a), poor fractures
(b), and medium number fractures (c) and a microfluidic chip with
two inlets and two outlets (d), representing formation with rich fractures.
Experiments of Gas Injection to Displace
Oil in Micromodel
As for gas injection to displace oil in
the actual reservoirs, there are various methods of gas injection,
such as gas injection from the edge of the oil formation, gas injection
from the top of the oil formation, gas injection from the edge of
the oil formation accompanied by water injection from the bottom of
the oil formation, etc. In order to investigate the oil displacement
behaviors of these three gas injection methods, the corresponding
three parallel experiments were conducted. Figure shows the schematic diagrams of these types
of gas injection methods and corresponding physical pictures of real
micromodels.
Figure 2
Schematic diagrams of gas injection from the edge of the
oil formation
(a), gas injection from the top of the oil formation (b), and gas
injection from the top of the oil formation and water injection from
the bottom of the oil formation (c) and the corresponding injection
methods (b, d, and f) in real micromodels.
Schematic diagrams of gas injection from the edge of the
oil formation
(a), gas injection from the top of the oil formation (b), and gas
injection from the top of the oil formation and water injection from
the bottom of the oil formation (c) and the corresponding injection
methods (b, d, and f) in real micromodels.Before all of the experiments, the porous media
were vacuumed and
were full of water. And then, the oil was injected into the micromodel
to saturate it until no water flowed out. During the first experiment,
the chip was placed horizontally, as shown in Figure b. Then, the gas was injected from the inlet,
and the produced fluid flowed out through the outlet. The injection
rate was 0.01 mL/min. This experiment was employed to simulate gas
injection from the edge of the oil formation. During the second experiment,
the micromodel was placed vertically, and then the gas was injected
through the inlet at the top of the micromodel. The produced fluid
flowed out through the outlet at the bottom of the micromodel. The
injection rate was 0.01 mL/min. This experiment was employed to simulate
gas injection from the top of the oil formation. During the third
experiment, the micromodel was placed vertically, and then the gas
was injected through the inlet at the top of the micromodel, while
the water was injected through the inlet at the bottom of the micromodel.
And the produced fluid flowed out through the outlets on either side
of the micromodel. The injection rate of gas and water was 0.005 mL/min.
This experiment was employed to simulate gas injection from the top
of the oil formation accompanied by water injection from the bottom
of the oil formation. The microscopic pictures were recorded by a
high-resolution microscope to observe the flow behaviors of gas and
oil in porous media. After the experiments, the pores and throats
were flushed by petroleum ether, ethanol, deionized water, and nitrogen
gas in turn. Finally, the chip was dried at a constant high temperature
of 60 °C for 12 h.
Results and Discussion
Gas Injection from the Edge of Porous Media
The sweep efficiency and oil displacement efficiency of the gas
injection from the edge of porous media is shown in Figure . Figure a and b showed that, as more gas was injected,
the swept area became larger and the oil production increased until
the injection volume reached 8 PV. Whether it is the sweep efficiency
or the oil displacement efficiency, the results showed that the porous
media with rich fractures kept the highest value and the porous media
with poor fractures kept the lowest value during the whole process.
The porous media with rich fractures represent oil formation with
well-developed fractures, high oil content, and high permeability.
In the process of gas flooding, the resistance is small and able to
spread to the distant pores and throats. Moreover, this phenomenon
is also reflected in the sweep efficiency and oil displacement efficiency
in areas of fractures and pores and throats. Due to the good connectivity
and width of fractures, the flooding effect of fractures was better
than those of pores and throats, as shown in Figure c and d. Under the method of gas injection
from the edge of porous media, the overall sweep efficiency was at
a relatively low level, and there was high risk of gas channeling
in areas of fractures.
Figure 3
Cumulative sweep efficiency (a) and oil displacement efficiency
(b) in different kinds of porous media as a function of gas injection
volume. The sweep efficiency and oil displacement efficiency of pores
and throats (c) and fractures (d) in different kinds of porous media
after gas injection from the edge of porous media.
Cumulative sweep efficiency (a) and oil displacement efficiency
(b) in different kinds of porous media as a function of gas injection
volume. The sweep efficiency and oil displacement efficiency of pores
and throats (c) and fractures (d) in different kinds of porous media
after gas injection from the edge of porous media.It is found through experiments that the activation
behaviors of
oil in three porous media are similar, so the gas injection from the
edge of porous media with rich fractures is mainly analyzed as shown
in Figure . In the
early stage of gas injection (<0.5 PV), the oil in fractures was
displaced first, with a fast speed and a rapid increase in oil production.
In the middle stage of gas injection (0.5–6 PV), more oil in
fractures was displaced, and at the same time the oil in a large number
of pores and throats around the fractures was displaced, resulting
in a relatively higher peak oil production. In the later stage of
gas injection (6–8 PV), a large amount of gas flowed along
fractures forming gas channeling, resulting in a large decrease in
displaced oil and a rapid decline in oil production. The fracture
is wider than the pores and throats, so the flow resistance of gas
in the fracture is lower, causing the initial gas to flow along the
fracture first, displacing the oil in the fracture region. Due to
the low density and high flowability, a part of subsequent gas could
invade into the tight pores and throats although they are narrow channels
under behaviors such as imbibition by virtue of low capillary resistance
of gas. The oil in pores and throats could be partially displaced
by the gas. Therefore, the gas invades the fractures first and then
invades the tight pores and throats to activate and displace the oil.
Figure 4
Displacement
process of oil in fractures, pores, and throats during
gas injection from the edge of porous media in a microfluidic chip
with rich fractures.
Displacement
process of oil in fractures, pores, and throats during
gas injection from the edge of porous media in a microfluidic chip
with rich fractures.The morphology of residual oil in porous media
after gas injection
from the edge of porous media with rich fractures, medium-number fractures,
and poor fractures is shown in Figure a–c, respectively. In porous media with rich
fractures, the formation of residual oil in swept areas was mainly
isolated residual oil and membranous residual oil. The membranous
residual oil refers to the residual oil attached to the wall surface
of fractures and the corner of pores. The isolated residual oil refers
to the residual oil in pores and throats separated by fractures. The
formation of residual oil in porous media with medium-number fractures
was similar to that of the porous media with rich fractures, involving
two types of residual oil: isolated residual oil and membranous residual
oil. However, the distribution of residual oil in porous media with
medium-number fractures was more correlated with the location of fractures,
which was caused by the sparsity of fractures. The residual oil in
areas without fractures was distributed continuously. In porous media
with poor fractures, the formation of residual oil in swept areas
was mainly slug-shaped residual oil. The reason for the formation
of slug-shaped residual oil was that the gas phase was cut off by
the oil and the residual oil was displayed as slug-shaped in fractures.
Because of the existence of high capillary force, it is difficult
for gas to enter the small pores and throats, and then it is difficult
to effectively displace the oil inside by gas.
Figure 5
Morphology of residual
oil in porous media after gas injection
from the edge of porous media in microfluidic chips with rich fractures
(a), medium-number fractures (b), and poor fractures (c).
Morphology of residual
oil in porous media after gas injection
from the edge of porous media in microfluidic chips with rich fractures
(a), medium-number fractures (b), and poor fractures (c).
Gas Injection from the Top of Porous Media
To inhibit gas channeling and thus enhance oil recovery, gas injection
from the top of porous media was studied, which is also considered
to be an effective method for developing some tight reservoirs with
fractures. The sweep efficiency and oil displacement efficiency of
gas injection from the top of porous media is shown in Figure . Compared with gas injection
from the edge of porous media, the overall sweep efficiency of gas
injection from the top of porous media increased about 5.4% to 9.9%,
and the overall oil displacement efficiency increased about 4.1% to
6.6%. Additionally, gas channeling was abated due to upward gas flow
caused by gravity, and thus the sweep efficiency and oil displacement
efficiency of pores and throats as well as fractures were improved
on average by approximately 7.2%, 4.1%, 1.5%, and 3.8%, respectively,
as shown in Figure d. After gas channeling was inhibited, displacement of residual oil
in pores and throats became more significant.
Figure 6
Cumulative sweep efficiency
(a) and oil displacement efficiency
(b) in different kinds of porous media as a function of gas injection
volume. The sweep efficiency and oil displacement efficiency of pores
and throats (c) and fractures (d) in different kinds of porous media
after gas injection from the top of porous media.
Cumulative sweep efficiency
(a) and oil displacement efficiency
(b) in different kinds of porous media as a function of gas injection
volume. The sweep efficiency and oil displacement efficiency of pores
and throats (c) and fractures (d) in different kinds of porous media
after gas injection from the top of porous media.According to the behavior of gas injection from
the top of porous
media, the sequence of gas flooding was similar to gas injection from
the edge of porous media, as shown in Figure . In the early stage of gas injection (<0.5
PV), the oil in fractures was displaced first. In the middle stage
of gas injection (0.5–4 PV), with the displacement of oil in
fractures, more oil in a large number of pores and throats around
the fractures was displaced. In the later stage of gas injection (4–8
PV), gas channeling formed, and there was a large decrease in oil
production. Although the oil recovery was improved when the gas injection
from the top was employed, gas channeling was still serious, and Figure shows that no matter
what kind of porous media, there was still a large amount of residual
oil left after gas flooding.
Figure 7
Displacement process of oil in fractures, pores,
and throats during
gas injection from the top of porous media in a microfluidic chip
with rich fractures.
Figure 8
Morphology of residual oil in porous media after gas injection
from the top of porous media in microfluidic chips with rich fractures
(a), medium-number fractures, (b) and poor fractures (c).
Displacement process of oil in fractures, pores,
and throats during
gas injection from the top of porous media in a microfluidic chip
with rich fractures.Morphology of residual oil in porous media after gas injection
from the top of porous media in microfluidic chips with rich fractures
(a), medium-number fractures, (b) and poor fractures (c).
Simultaneous Injection of Gas and Water from
the Top of Porous Media and the Bottom of Porous Media, Respectively
Simultaneous injection of gas and water from the top of porous
media and the bottom of porous media, respectively, was studied to
enhance the oil recovery of gas flooding. According to the displacement
results of simultaneous injection of gas and water from the top of
porous media and the bottom of porous media, respectively, shown in Figure , all areas of fractures
were swept and the oil in pores and throats around fractures was started
and displaced when the injection volume of gas was 4 PV. When 8 PV
gas was injected into porous media, the swept area was further expanded,
and the oil recovery reached near the top. Simultaneous injection
of gas and water from different locations significantly improved the
oil recovery. Compared with the gas injection from the top of porous
media, this injection method displayed more effective displacement
of oil. The overall sweep efficiency and the overall oil displacement
efficiency increased about 18.4% and 13.4%, respectively. This suggested
that the combining gas flooding and water flooding showed an optimal
enhanced oil recovery effect compared with the gas injection. Simultaneous
injection of gas and water from the top of porous media and the bottom
of porous media, respectively, is an optimized enhanced oil recovery
method.
Figure 9
Sweep efficiency and oil displacement efficiency of pores and throats,
fractures, and the whole porous media in porous media with rich fractures
after simultaneous injection of gas and water from the top of porous
media and the bottom of porous media, respectively.
Sweep efficiency and oil displacement efficiency of pores and throats,
fractures, and the whole porous media in porous media with rich fractures
after simultaneous injection of gas and water from the top of porous
media and the bottom of porous media, respectively.The better displacement effect of the combining
gas and water injection
can be included for three reasons. It can be seen from microscopic
displacement images shown in Figure . First, gas can invade deep pores and throats that
are difficult for water to enter, as shown in Figure a. Second, compared with gas, the viscosity
of water is higher, and thus the water shows a relatively smaller
mobility. Therefore, water flooding sweeps a larger area than pure
gas flooding. Moreover, in gas–water mixing regions, two-phase
flow resistance is larger than single phase, which inhibits channeling
and increases the swept range. It is suggested to inject gas from
a higher location and inject water from a lower location to enhance
the oil recovery.
Figure 10
Oil was displaced by gas (a), water (b), and the mixture
of gas
and water (c) during the oil displacement by simultaneous injection
of gas and water from the top of porous media and the bottom of porous
media, respectively.
Oil was displaced by gas (a), water (b), and the mixture
of gas
and water (c) during the oil displacement by simultaneous injection
of gas and water from the top of porous media and the bottom of porous
media, respectively.
Conclusions
In this study, enhanced
oil recovery methods for gas injection
of fractured reservoirs were explored by microfluidic technology.
The primary conclusions drawn from this study are summarized as follows.(1) In the process of gas injection, there are three stages of
gas displacing oil. In the early stage of gas flooding, the oil in
fractures was quickly displaced first. In the middle stage of gas
flooding, more oil in fractures was displaced, and at the same time
the oil in pores and throats around the fractures was displaced. In
the later stage of gas flooding, gas channeling mainly occurred in
fractures, and very little oil was displaced out OF the porous media.(2) The sweep efficiency and oil displacement efficiency showed
a tendency of increasing first and then stabilizing. The sweep efficiency
and oil displacement efficiency of fractures were much higher than
those of pores and throats. And the channeling inhibition ability
of gas injection from the top of porous media was more prominent,
which was beneficial to delaying gas channeling occurrence.(3) Simultaneous injection of gas and water from the top of porous
media and the bottom of porous media, respectively, showed an optimal
enhanced oil recovery effect among these three injection methods,
which could be attributed to three main reasons. First, gas can invade
deep and small pores and throats that are difficult for water to sweep.
Second, the viscosity of water is higher than that of gas, endowing
water a relatively smaller mobility to sweep a larger area than pure
gas flooding. Third, the channeling in the gas–liquid two-phase
mixing region was inhibited more obviously(4) Compared with
single phase flooding, the method of gas injection
from the top and water injection from the bottom inhibits the channeling
of gas more effectively in fractured reservoirs. The overall sweep
efficiency and the overall oil displacement efficiency increased about
18.4% and 13.4%, respectively.