Primary
oil recovery from fractured unconventional formations,
such as shale or tight sands, is typically less than 10%. The development
of an economically viable enhanced oil recovery (EOR) technique applicable
to unconventional liquid reservoirs (ULRs) would lead to tremendous
increases in domestic oil production. Although injection techniques
such as waterflooding and CO2 EOR have proven profitable
in conventional formations for decades, EOR in ULRs presents a far
more difficult challenge. The extremely low permeability and mixed
wettability of unconventional formations are the foremost obstacles
to success. Because of the challenges associated with water-based
EOR techniques (a.k.a., chemical EOR) in shale, several nonaqueous
injection fluids have been considered, including CO2, natural
gas, and (to a lesser degree) nitrogen. All these fluids have significantly
lower viscosities than water, allowing them to more easily penetrate
shale nanopores. Unlike water, they also each possess some degree
of miscibility with oil, which enables the gas to extract oil through
a combination of mechanisms. Based on laboratory-scale experimentation,
CO2 and rich natural gas (methane-rich natural gas containing
high concentrations of ethane, propane, and butane) are the most promising
EOR fluids. The interpretation of results from field tests in the
Bakken and Eagle Ford formations have been complicated by interference
of frac-hits or well-bashing caused by hydraulic fracturing at nearby
wells. In this review we cover mechanisms, laboratory experiments,
numerical simulations, and field tests involving high-pressure CO2, natural gas, ethane, nitrogen, and water.
In this study, contact
angles were measured for CO2 bubbles
on six different sandstones (Navajo, Nugget, Bentheimer, Bandera Brown,
Berea, and Mt. Simon) that could potentially represent properties
of CO2 storage depositional environments. The impacts of
pressure and temperature were studied by focusing on the CO2 phase behavior in three different scenarios: gaseous, liquid, and
supercritical conditions. Despite controlling the sample preparation
and cleanliness, CO2–brine equilibration conditions,
and pressure and temperature, there were inconsistencies in contact
angle trends that could largely be attributed to natural sample heterogeneity
resulting from localized variations in topography, surface roughness,
and mineral composition across the surface. Despite these variations,
the analysis of 298 measurements from this study showed that 81% of
the contact angles were <40°, representing strongly water-wet
to (moderately) water-wet behaviors. Also, 17.3% of the measurements
were between 40° and 60° (weakly water-wet) and primarily
belonged to small CO2 bubbles (<500 μm) that were
heavily impacted by localized surface heterogeneity in natural sandstone
samples. In addition, only 1.7% of the measurements had angles greater
than 60° and could be classified as no longer water-wet, but
these measurements occurred on extremely small bubbles (100–200
μm) that were very dependent on localized surface heterogeneity.
While some of the detailed physics of the CO2/brine/sandstone
interface is still poorly understood, from an application standpoint,
the sandstones of this study were best characterized as strongly water-wet
to (moderately) water-wet.
CO2 injection is a promising method for enhanced
oil
recovery (EOR) in unconventional shale reservoirs. In this work, we
postulate that CO2 EOR may be improved by the dissolution
of surfactants into CO2. Although CO2 is a relatively
good solvent for oil, we show that CO2 and Eagle Ford oil
are immiscible at compositions above 70 wt % CO2, even
at pressures as high as 62 MPa. The presence of a CO2–oil
interface at reservoir conditions indicates that the addition of a
surfactant has the potential to improve oil recoveryvia wettability
alteration from oil-wet to CO2-wet, CO2–oil
interfacial tension (IFT) reduction, or both. Three nonionic surfactants
(branched tridecyl ethoxylate Indorama SURFONIC TDA-9, branched nonylphenol
ethoxylate Indorama SURFONIC N-100, and linear dodecyl ethoxylate
Indorama SURFONIC L12-6) were evaluated for CO2-solubility,
shale wettability alteration, effect on CO2–oil
IFT, ability to generate CO2–oil foams, and ability
to increase oil extraction from Eagle Ford, Mancos, and Bakken shale
cores. Each surfactant dissolved in CO2 up to 1 wt % at
pressures and temperatures commensurate with CO2 EOR. CO2-dissolved surfactants did not significantly affect CO2–oil IFT or generate CO2–oil foams,
but they did induce a dramatic change in the contact angle of an oil
droplet on an oil-aged shale chip in CO2 from strongly
oil-wet (11°) toward intermediate CO2–oil wettability
(82°) (at 80 °C, 27.6 MPa). The branched tridecyl ethoxylated
surfactant, SURFONIC TDA-9, afforded the highest oil recovery in core
soaking experiments75%, compared to 71% by pure CO2. Analysis of oil extracts by gas chromatography revealed that heavier
oil components were produced when the surfactant was added to CO2. These results indicate that CO2-dissolved surfactants
may increase oil recovery from shale by wettability alteration from
oil-wet toward CO2-wet.
Free energy of nanoparticles
can increase the surface activity
at the solid/oil/liquid contact line and remove oil through the disjoining
pressure gradient mechanism. Surfactants can also remove oil mainly
by reducing interfacial tension, although raising economic concerns
as a result of their adsorption on the rock surface. Introduction
of nanoparticles to surfactant solutions seemed to be more prominent
in improving the wettability than reducing the interfacial tension,
which could offer an opportunity to develop cost-effective chemical
flooding agents to enhance oil recovery in carbonate reservoirs. However,
characterization of wettability alteration using contact angles typically
fails in providing consistent results. In this study, the dual-drop–dual-crystal
technique was employed to measure precise and reproducible dynamic
contact angles and was supported by relative permeability curves generated
by coreflood experiments to evaluate the wettability alteration performance
of silica nanoparticles combined with both effective and ineffective
anionic surfactants at both ambient and high-pressure, high-temperature
conditions. Adding nanoparticles to surfactants was seen to change
the wettability of the carbonate rocks from strongly oil-wet to weakly
oil-wet and intermediate-wet conditions (e.g., change in the advancing
contact angle from 167° to 98°), which improved the oil
recovery (up to 93% of the original oil in place) and reduced the
residual oil saturation, without having to significantly reduce the
interfacial tension (only 1 or 2 orders of magnitude). Reduction of
the surfactant concentration in the combination did not significantly
hinder the wettability alteration performance, showing the ability
of nanoparticles to compensate for surfactants. Therefore, the combination
of nanoparticles and low-cost dilute surfactants can be tuned to provide
economically appealing chemical flooding agents to enhance oil recovery.
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