Ahmed M Saad1, Stefano Aime2,3, Sharath Chandra Mahavadi4, Yi-Qiao Song4,5, Maxim P Yutkin1, David Weitz2,6, Tadeusz W Patzek1. 1. Ali I. Al-Naimi Petroleum Engineering Research Center, King Abdullah University of Science and Technology, Thuwal 23955-6900, Saudi Arabia. 2. John A. Paulson School of Engineering and Applied Sciences, Harvard University, Cambridge, Massachusetts 02138, United States. 3. Molecular, Macromolecular Chemistry, and Materials, ESPCI Paris, CNRS, PSL University, 10 Rue Vauquelin, Paris 75005, France. 4. Schlumberger-Doll Research, One Hampshire Street, Cambridge, Massachusetts 02139, United States. 5. Athinoula A. Martinos Center for Biomedical Imaging, Department of Radiology, Massachusetts General Hospital, Charlestown, Massachusetts 02129, United States. 6. Department of Physics, Harvard University, Cambridge, Massachusetts 02138, United States.
Abstract
We investigate the formation and properties of crude oil/water interfacial films. The time evolution of interfacial tension suggests the presence of short and long timescale processes reflecting the competition between different populations of surface-active molecules. We measure both the time-dependent shear and extensional interfacial rheology moduli. Late-time interface rheology is dominated by elasticity, which results in visible wrinkles on the crude oil drop surface upon interface disturbance. We also find that the chemical composition of the interfacial films is affected by the composition of the aqueous phase that it has contacted. For example, sulfate ions promote films enriched with carboxylic groups and condensed aromatics. Finally, we perform solution exchange experiments and monitor the late-time film composition upon the exchange. We detect the film composition change upon replacing chloride solutions with sulfate-enriched ones. To the best of our knowledge, we are the first to report the composition alteration of aged crude oil films. This finding might foreshadow an essential crude oil recovery mechanism.
We investigate the formation and properties of crude oil/water interfacial films. The time evolution of interfacial tension suggests the presence of short and long timescale processes reflecting the competition between different populations of surface-active molecules. We measure both the time-dependent shear and extensional interfacial rheology moduli. Late-time interface rheology is dominated by elasticity, which results in visible wrinkles on the crude oil drop surface upon interface disturbance. We also find that the chemical composition of the interfacial films is affected by the composition of the aqueous phase that it has contacted. For example, sulfate ions promote films enriched with carboxylic groups and condensed aromatics. Finally, we perform solution exchange experiments and monitor the late-time film composition upon the exchange. We detect the film composition change upon replacing chloride solutions with sulfate-enriched ones. To the best of our knowledge, we are the first to report the composition alteration of aged crude oil films. This finding might foreshadow an essential crude oil recovery mechanism.
Multicomponent fluids
exhibit rich and complex interfacial properties,
dictated by each component’s mobility and chemical nature.
Relating the mechanical properties of complex interfaces to the composition
of the bulk materials is vital for many applications, from chemical
engineering and food science to biology and medicine.[1] In particular, the interfacial properties of crude oil
have received significant attention over the past decades because
of their relevance to oil recovery, transport, and processing.[2−4] For example, most oil extraction processes are based on injecting
water-based liquids, called brines, into the porous oil reservoir.
The efficiency of this process, known as waterflooding, is generally
understood as an interplay between viscous and interfacial forces,
and it has been shown that it can be enhanced by tuning the chemical
composition of the brine, for example, by reducing its salinity or
by selectively increasing the concentration of certain divalent ionic
species.[5−9] However, despite intense research in this field, the underlying
mechanisms that lead to improved oil recovery are still debated.[10−21] Moreover, the complex rheology of the interfacial films dictates
the stability of oil/water emulsions, with implications in oil transport,
processing, and final quality.[22,23]For these reasons,
adsorption of surface-active moieties at the
crude oil-water interface has been extensively studied in the past
decades. However, the vast majority of these studies focus only on
the measurement of interfacial tension, γ, while the mechanical
properties of crude oil–water interfaces may be more complex
and require a thorough rheological characterization.[24,25] Interfacial rheology experiments have highlighted, for instance,
that many elementary processes, from drop coalescence to snap-off
inside rock pores, are often strongly affected by the elasticity of
the interfacial film.[13,26,27] Nevertheless, such experiments remain scarce, and their interpretation
is controversial due to the lack of a clear connection between the
mechanical properties observed in experiments and the underlying physicochemical
processes.In this paper, we investigate the evolution of the
interface between
crude oil and solutions of different chemical compositions by measuring
the interfacial tension as well as the complex shear and extensional
viscoelastic moduli of the interface. We find that the formation of
interfacial films is nontrivially affected by the chemical composition
of the water phase. Furthermore, we analyze the functional groups
contributing to the formation of the films using Fourier transform
infrared (FTIR) spectroscopy. We show that the ionic species present
in the aqueous phase impact not only the rheology of the interfacial
films but also their chemical composition. Our study indicates that,
among all molecular species in crude oil, polar aromatic molecules
are critical for the formation of viscoelastic interfacial films and
that sulfate salts are particularly efficient in promoting their adsorption
at the interface, thereby producing more elastic films. Moreover,
we show preliminary evidence that this adsorption process is partially
reversible and that the properties of fully developed interfacial
films can be tuned by changing the composition of the aqueous phase.
These results set the basis for a deeper understanding of the chemical
origin of the interfacial rheology of complex crude oil systems.
Materials and Methods
Chemicals
Deionized
(DI) water was obtained from a
Milli-Q water purification system (Synergy, EMD Millipore Corporation),
which produces type I water with a resistivity greater than 18.2 MΩ
cm at 25° C and total organic content less than 10 ppb. The salt
used is ACS reagent, ≥99.0%, from Fisher Scientific. Toluene
(99.9%, Fisher Scientific) for crude oil dilution was used as received.
Crude oil was received from Schlumberger. Its saturate, aromatic,
resin, and asphaltene (SARA) composition was obtained using the IP-143
method[28] and is presented in Table along with other physical and
chemical properties relevant for this study. In most of our experiments,
we used a 3% w/w crude oil solution in toluene. The dilution reduces
crude oil viscosity, eases the handling, and allows working with a
limited amount of the available sample. To promote dilution, the two
fluids were mixed using a vortex mixer for 1 min.
Table 1
SARA Composition and Physical Properties
of Crude Oil
property
crude
oil
saturates [wt %]
38.3
aromatics [wt %]
19.8
resins [wt %]
36.6
asphaltene [wt %]
3.97
total acid number [mg KOH/g]
1.19
density @ 25 C° [g/cm3]
0.955
viscosity [cP]
1290
Interfacial Rheology
We probe the mechanical properties
of the interfacial films using both dilational and shear interfacial
rheology. Dilational rheology experiments are performed using an optical
tensiometer (Biolin Theta Flex TF300 with PD200 oscillating drop module),
where an oil droplet is formed at the tip of a 14 gauge inverted needle
inside a 30 mL glass cell filled with the aqueous phase. The droplet
volume is periodically modulated with a prescribed amplitude and frequency
using an automated syringe pump and a piezo pump. A camera records
the droplet shape, which is then analyzed to obtain the time-dependent
surface area, A(t), dynamic interfacial
tension, γ(t), and complex interfacial modulus, Es*.[29] A strain amplitude
of 0.5% and a frequency of 0.1 Hz were used for all dilational rheology
experiments. The first measurement starts 5 s after complete droplet
inflation to the desired volume.Shear rheology experiments
are performed using a Discovery Hybrid Rheometer from TA Instruments,
equipped with a Double Wall Ring interfacial geometry. A commercial
double wall ring cell was customized with homemade components, as
shown in the Supporting Information (Figure
S1), to reduce the evaporation of volatile components in crude oil
and toluene during experiments lasting several days.[30] In addition, our shear rheology setup allows us to wash
the bulk oil phase at the end of the experiment using pure toluene
without disrupting the interfacial film, thereby enabling the collection
of the interfacial material. All shear rheology experiments were performed
at 0.1% strain amplitude and 1 Hz frequency. The choice of amplitude
and frequency for both shear and dilational rheology is further discussed
in the Supporting Information (Figures
S2, S3).
FTIR Spectroscopy
To examine the chemical composition
of the interfacial films, we recorded the FTIR spectra of the interfacial
films collected from the oil–water interfaces. The interfacial
material was collected using a procedure described in detail elsewhere.[31,32] Here, we provide the key details for the reader and a schematic
of the process (see Supporting Information, Figure S9). The interfacial material was formed by layering a crude
oil–toluene mixture (3% vol) on top of an aqueous solution
in a wide glass dish to maximize the contact area. After the layering,
the organic material in the crude oil–toluene mixture was allowed
to adsorb at the toluene–water interface for 24 h. Afterward,
the toluene phase was removed by repeated dilution, followed by decantation.
Eventually, pure toluene on top of the interfacial material was allowed
to evaporate, and the interfacial material was collected from the
water–air interface by a Teflon spatula. Then, the collected
material was dissolved in dichloromethane. The dichloromethane solution
was deposited dropwise on the ATR crystal of an FTIR spectrometer.
After the evaporation of dichloromethane, FTIR spectra were recorded
using a Varian 670-IR FTIR spectrometer in the attenuated total reflectance
(ATR) mode with MIRacle ATR accessory from PIKE Technologies. All
measurements were performed under a nitrogen blanket.
Results
and Discussion
Adsorption Kinetics
We study the
adsorption kinetics
at the crude oil–water interface by monitoring the time evolution
of the surface tension, γ(t), using a pendant
drop apparatus. When the interface is formed against a deionized water
phase, we find that γ(t) starts from a short-time
value γ0 of about 28 mN/m and decays logarithmically
in time, without approaching a well-defined steady state within the
24 h time window probed by experiments, as shown by the black data
points in Figure .
This indicates that the adsorption and equilibration of surface-active
molecules at the interface is an extremely slow process, characterized
by timescales much beyond those set by the mobility of molecules in
the bulk phases. Such slow dynamics suggests that this regime is dominated
by molecular interactions, which hinder molecular migration and reorganization
at the interface.[33,34]
Figure 1
Adsorption kinetics. Interfacial tension,
γ, plotted against
time, t, since droplet formation, varying (a) salt
chemistry, at fixed salt concentration (0.1 M) and crude oil concentration
(3%); (b) salt concentration, cNaCl, for
fixed salt chemistry (NaCl) and crude oil concentration (3%); (c)
crude oil concentration, cc (w/w, in toluene),
for fixed aqueous phase (0.1 M NaCl); (d) effect of equilibration
protocol, for fixed aqueous phase (1 M NaCl) and oil concentration
(3%). The first measurement is recorded 5 s after the initial droplet
inflation to the desired size. The top labels mark the three steps
of film formation [(I) t < 0.18 h, early stage;
(II) 0.18 h < t < 8 h, film formation; (III) t > 8 h, network
aging].
Adsorption kinetics. Interfacial tension,
γ, plotted against
time, t, since droplet formation, varying (a) salt
chemistry, at fixed salt concentration (0.1 M) and crude oil concentration
(3%); (b) salt concentration, cNaCl, for
fixed salt chemistry (NaCl) and crude oil concentration (3%); (c)
crude oil concentration, cc (w/w, in toluene),
for fixed aqueous phase (0.1 M NaCl); (d) effect of equilibration
protocol, for fixed aqueous phase (1 M NaCl) and oil concentration
(3%). The first measurement is recorded 5 s after the initial droplet
inflation to the desired size. The top labels mark the three steps
of film formation [(I) t < 0.18 h, early stage;
(II) 0.18 h < t < 8 h, film formation; (III) t > 8 h, network
aging].As salts are added to the aqueous
phase; however, γ(t) develops a very unusual,
nonmonotonic decay: at the earliest
times experimentally accessible, we find that it starts from a relatively
low value γ0, then starts rising, and subsequently
joins the logarithmic decrease, typical of DI water–oil interfaces.
We observe that this first nonmonotonic transient regime depends on
the water chemistry, with different salts associated with different
γ0, as shown in Figure a. To confirm this hypothesis, we study the
impact of salt concentration, and we find that, as expected, larger
salt concentrations are associated with a lower γ0, as shown in Figure b. Such nonmonotonic behavior of γ(t) is rather
unusual, as it implies that the total surface energy spontaneously
undergoes a transient growth. Our data show that all γ(t) curves start raising at the same time, joining the DI
water curve at time tI ≈ 10 min,
quite independent of salt chemistry and concentration. Thus, because
the timescale associated with this growth is independent of the chemical
composition of the water phase, we investigate the role of the oil
phase by fixing the water phase to 0.1 M NaCl solution and changing
the concentration of crude oil in toluene, cc. As cc is decreased, we find
that the transient increase in γ(t) becomes
slightly slower and less pronounced, and it disappears completely
for the lowest value of cc tested, as
shown in Figure c.
By contrast, the decay of γ(t) for t > tI becomes much faster
for
lower cc. A similar early-time nonmonotonic
behavior has been reported in the literature for crude oil,[35−37] but to the best of our knowledge, no detailed explanation has been
proposed so far.To understand this behavior, we consider the
complex, multicomponent
nature of crude oil, composed of a wide spectrum of chemical species
of different sizes, polarity, and mobility. Among the molecules containing
polar groups, thus susceptible to adsorption at the oil–water
interface, we schematically isolate the contribution of two families
of molecules: (A) small molecules, with the polar head connected to
a relatively small hydrophobic tail and (B) large molecules, with
the polar groups bound to a larger hydrophobic body. Being characterized
by larger mobility, (A) molecules adsorb faster at the interface,
dictating the short-time value of γ0. The presence
of ionic species in the water phase favors the deprotonation of the
acid groups of the adsorbed molecules, thereby increasing the energy
gain for adsorption. This results in faster adsorption kinetics and
thus a faster drop in γ(t) at very early times
before the first experimental point is measured. The dependence of
γ0 on the salt chemistry then stems from the effect
of each salt species on the adsorption energy, with the divalent cation
(Ca2+) associated to the largest decrease in γ0, indicative of a larger energy gain, followed by Na2SO4, which provides twice as many monovalent cations (Na+) as NaCl at equal molarity. However, because of their comparatively
short hydrophobic tail, (A) molecules may be partially soluble in
the water phase, depending on its salinity.[38−40] Thus, at later
times, (A) molecules adsorbed at the interface may partition in the
water phase, leading to an increase in γ(t),
leaving some room for the adsorption of (B) molecules. This second
process is much slower, as the mobility of (B) molecules is further
hindered by their size and intermolecular interactions.[33,34,41,42]To test this model, we measure γ(t)
in the
oil–water systems that have previously been in contact, such
that the partitioning of (A) molecules has occurred prior to the droplet
formation. To this end, we presaturate the aqueous phase by multiple
extractions of the water-soluble components. Saturation is obtained
by keeping the water and oil phases in contact for 15 min with intermittent
shaking and by subsequently replacing the oil phase with a fresh sample.
This process is repeated five times, after which the bulk phases are
extracted. We investigate another condition that we refer to as equilibrated,
where the two fluids are kept in contact and shaken for 15 min only.
Eventually, we inflate a droplet of either saturated or equilibrated
crude oil sample surrounded by the saturated water phase. The resulting
γ(t) exhibits in both cases a monotonic logarithmic
decrease, as shown in Figure d, confirming that the transient growth in γ(t) is indeed related to the partitioning of (A) molecules
into the water phase.At the latest stages of the experiments,
we find that if the salinity
of the water phase is large enough, γ(t) deviates
once again from the logarithmic decay found for DI water and exhibits
a faster decay. This suggests the onset of an even slower process
around tII ≈ 8 h: we anticipate
that it corresponds to the formation of an elastic interfacial skin,
as we shall see in the next section.
Rheology of the Interfacial
Films
As we deflate the
droplet by withdrawing the syringe after the development of γ(t) for 24 h, we find that the droplet does not shrink homogeneously:
instead, its surface develops wrinkles, as shown in Figure a. This indicates that molecules
that adsorb at the interface interact with each other to form a solid
skin.[43] To characterize the mechanical
properties of this skin, we perform time-resolved dilational rheology
experiments on the droplet. To this end, we use a piezo pump to impose
a small periodic perturbation at frequency ω = 0.1 Hz to the
volume of the droplet, and we record its subsequent change in shape.
This enables the measurement of the complex dilational modulus Es*(ω) of the interface, describing the
mechanical stress associated with its periodic extensional deformation.[29] We find that the mechanical response is largely
dominated by the real part of Es*, which
is the elastic dilational modulus, Es′,
describing the stress component in phase with the applied deformation
(see Supporting Information, Figure S4).
Furthermore, we find that Es′ grows
logarithmically in time for all samples tested, as shown by the full
symbols in Figure b.
Figure 2
Rheology of interfacial films. (a) Snapshot of a wrinkled droplet
surface produced as the droplet is deflated after long-time skin formation
(24 h) in contact with DI water. (b) Extensional elastic modulus (Es′, squares, left axis) and shear elastic
modulus (Gs′, solid lines, right
axis) as a function of time for varying salt chemistry, at fixed salt
concentration (0.1 M) and crude oil concentration (3%). Colors indicate
salt chemistry, as in Figure a. (c–e) Equation-of-state exponent, p, for different salt species (c), salt concentration (d), and crude
oil concentration (e).
Rheology of interfacial films. (a) Snapshot of a wrinkled droplet
surface produced as the droplet is deflated after long-time skin formation
(24 h) in contact with DI water. (b) Extensional elastic modulus (Es′, squares, left axis) and shear elastic
modulus (Gs′, solid lines, right
axis) as a function of time for varying salt chemistry, at fixed salt
concentration (0.1 M) and crude oil concentration (3%). Colors indicate
salt chemistry, as in Figure a. (c–e) Equation-of-state exponent, p, for different salt species (c), salt concentration (d), and crude
oil concentration (e).The remarkable overlap
of all Es′(t),
together with their logarithmic time dependence, resembles
that of γ(t) in the intermediate regime of
film formation, as shown in Figure a. The analogy between the two quantities suggests
that here Es′ is dominated by Gibbs
elasticity, which describes the dependence of γ on the surface
coverage, Γ. Indeed, the periodic modulation in the surface
area applied to measure Es′ entails
a periodic modulation of surface coverage, which reflects in the time-dependent
surface tension that effectively contributes to the measured elastic
modulus. This contribution is called the Gibbs modulus,[44]EG = −dγ/d
ln Γ, and provides information on the equation of state γ(Γ).
An analytic solution for γ(Γ) can be derived by recognizing
that Es′(t) is
proportional to the interfacial tension decay, δγ(t) = γ(t) – γr, with γr being
a reference tension representative of the naked interface. Under the
working hypothesis that EG ≈ Es′ = −pδγ,
with p a sample-dependent constant prefactor, we
obtain a differential equation in δγ(Γ): d ln δγ/d
ln Γ = p. The solution of this equation is
a power-law dependence on surface coverage: Es′ ∝ δγ ∝Γ.To extract the characteristic exponent, p, from
our experimental data, we fit both Es′(t) and γ(t) for tI < t < tII to the logarithmic growth and decay, respectively. The fits
yield a characteristic time, τ, such that Efits′(τ)
= 0, and a reference surface tension, γr = γfit(τ). From this, we calculate δγ(t), and we extract p = ⟨−Es′/δγ⟩, where ⟨···⟩ denotes averaging over all data points in the
regime where logarithmic dependence is observed (see Supporting Information, Figure S5). By repeating this analysis
on all measured samples, we find that p depends weakly
on salt chemistry and decreases with both increasing salt concentration
and decreasing oil concentration, as shown in Figure c–e. This result highlights the physical
meaning of p: a smaller p reflects
a weaker dependence of Es′ and
γ on surface coverage. Thus, in analogy to 3D bulk systems,[45] we interpret p as a measurement
of the softness of the interface, smaller p representing
softer interfaces. This softness may be attributed to intermolecular
interactions, which promote clustering at the interface, inhibiting
the molecular restructuring required to increase the surface coverage
further. Indeed, from the logarithmic decay of δγ(t), we find that Γ(t) ∝ [ln(t/τ)]1/, implying that
larger p entails a slower evolution of Γ(t). In these terms, the increase of p with cc, shown in Figure e, suggests that larger oil concentration
yields faster and more disordered crowding at the interface, whereas
the decrease of p with cNaCl, shown in Figure d, suggests that larger salt concentrations favor molecular ordering,
as found in some surfactant systems.[46] Thus,
this notion of interfacial softness efficiently accounts for our experimental
results. In addition, the weaker dependence of p on
salt chemistry, shown in Figure c, suggests that intermolecular interactions depend
on salt chemistry, with weaker interactions in the case of chloride
salt films; this is key to understanding the onset of complex interfacial
rheology.In fact, while the Gibbs elasticity is useful to derive
the equation
of state γ(Γ), it does not inform on the deviatoric surface
stresses leading to wrinkles and crumpling of the droplet skin.[47,48] Indeed, we observe that the oil droplet retracts smoothly if the
liquid is withdrawn before tII, whereas
it develops wrinkles, shown in Figure a, when oil is withdrawn during the latest stage of
film formation, where Es′ is no
longer proportional to δγ. To study the onset of these
deviatoric surface stresses, we use shear interfacial rheology, which
probes the complex shear modulus of the interface, Gs*(ω). Because it describes the mechanics of the
interface at a constant surface area, Gs*(ω) is completely insensitive to surface tension. We find
that its absolute value is below the sensitivity limit of the instrument
(about 0.1 mN/m) throughout the first two phases of film formation
and only becomes measurable during the third phase. In this phase,
we find that Gs*(ω) is dominated
by its real part, Gs′, which is
the shear storage modulus, and is shown as thick solid lines in Figure b. The shear modulus
shows a strong dependence on the aqueous phase chemistry with DI water
and Na2SO4 films, developing a measurable Gs′ first. The chloride salt films show
a delayed onset of shear elasticity, with no measurable modulus in
the case of the CaCl2 film during the timescale of the
experiment. This is in agreement with the lower p observed in Figure , and it is in contrast to the early-time evolution of γ(t), for t < tI, which was rather dictated by the amount and valency of the cations,
Na+ and Ca2+, with little or no impact of the
anions, Cl– and SO42–. This contrast further confirms that the initial adsorption and
the formation of the interfacial skin at longer times are independent
processes. A deeper understanding of these mechanisms may help in
rationalizing the results reported in the literature about wettability
alteration and efficiency of oil recovery, for which no robust explanation
has been proposed.[10,49]
Chemical Composition of
the Interfacial Films
To understand
the origin of this complex rheology and the differences between interfacial
films produced with different salts, we analyzed the chemical composition
of the interfacial material using FTIR. To highlight the specificity
of adsorbed molecules, we first compare the composition of interfacial
materials with that of bulk crude oil, shown as a dashed gray line
in Figure a. We find
that for bulk crude oil, the spectrum is dominated by a pair of pronounced
peaks around 1400 cm–1, coming from methyl and methylene
groups, with a shallower peak at 1600 cm–1, indicating
the presence of aromatic C=C bonds. There is no significant
signature of any other functional groups, in line with the composition
reported in Table , dominated by saturates and aromatics. By contrast, interfacial
materials exhibit richer spectra, shown as solid lines in Figure a, with different
colors reflecting different aqueous phase chemistries. With respect
to bulk crude oil, they all exhibit an additional peak around 1730
cm–1, which corresponds to the stretching of the
C=O bond of carbonyl groups and indicates that interfacial
materials are enriched with polar carboxylic acid groups.[31] In addition, interfacial materials have enhanced
spectra in the so-called fingerprint region, between 650 and 1200
cm–1. In particular, we focus on the range between
650 and 950 cm–1, which is expanded in Figure b, highlighting the
degree of condensation and substitutions on the aromatic groups. In
this region, we identify five peaks, marked by labels 1H, ..., 5H,
which correspond to aromatic rings with one to five neighboring hydrogen
atoms, as schematically illustrated in Supporting Information, Figure S11. In addition, our spectra exhibit a
pronounced peak at 727 cm–1, which indicates the
presence of long aliphatic chains (CH2) almost invisible in bulk crude oil. Despite these common
features, the FTIR spectra of interfacial materials produced against
solutions with different chemical compositions exhibit quantitative
differences, suggesting that the aqueous phase chemistry does impact
the film composition. In particular, we find that NaCl and CaCl2 produce similar spectra (red and green lines in Figure ), whereas Na2SO4 (blue line) forms interfacial films with a
quite different chemical composition, more enriched in carboxylic
acids and highly condensed aromatics, as shown by the enhanced C=O
peak and fingerprint peaks, respectively. This suggests that the chemical
nature of the counterions, Cl– and SO42–, has a stronger impact on the properties of
the interfacial materials than the valency of cations, in agreement
with the rheology data shown in Figure .
Figure 3
Chemical composition of interfacial films. (a) FTIR spectra
of
interfacial films and bulk crude oil between 550 and 1850 cm–1, highlighting the acid region (1550–1800 cm–1) and the fingerprint region (650–750 cm–1). (b) Fingerprint region of the spectra showing the peaks corresponding
to different substitutions of aromatic rings (number of adjacent hydrogen
atoms) as well as the peak corresponding to the alkyl chain with more
than four carbons. (c) Concentration of carboxylic acid group relative
to the C=C peak (1600 cm–1), obtained as
the integral areas of the deconvoluted peaks. (d) Concentration of
aromatic moieties relative to the (CH2) peak (727 cm–1) of long alkyl chains.
Chemical composition of interfacial films. (a) FTIR spectra
of
interfacial films and bulk crude oil between 550 and 1850 cm–1, highlighting the acid region (1550–1800 cm–1) and the fingerprint region (650–750 cm–1). (b) Fingerprint region of the spectra showing the peaks corresponding
to different substitutions of aromatic rings (number of adjacent hydrogen
atoms) as well as the peak corresponding to the alkyl chain with more
than four carbons. (c) Concentration of carboxylic acid group relative
to the C=C peak (1600 cm–1), obtained as
the integral areas of the deconvoluted peaks. (d) Concentration of
aromatic moieties relative to the (CH2) peak (727 cm–1) of long alkyl chains.This analogy further motivates the search for the
chemical origin
of the mechanical properties of our interfacial films. To this end,
we estimate the relative concentrations of different functional groups
through deconvolution by fitting the FTIR spectra to a sum of Gaussian
curves. We then estimate the relative amount of each functional group
by summing over the areas of all curves within the expected range
of wavenumbers. To properly account for different sample volumes and
for the absorbance coefficients of different functional groups, we
normalize our results by the area of the C=C peak, which we
take as a reference signal. Details of the fitting protocol and results
are given in Supporting Information, Section
S6. We find that the relative amount of carboxylic acid groups is
several times larger in films formed against Na2SO4 than in the others, as shown in Figure c. In addition, we observe that the detailed
shape and position of the C=O peak differs from sample to sample.
We interpret this as a result of the heterogeneous chemical environment
surrounding the C=O bond, whose absorption peak shifts toward
smaller wavenumbers when the carbonyl group is either in conjugation
with a double bond or an aromatic group or H-bonded with another molecule.[50] Therefore, we classify the contribution of the
carbonyl group as bound, or conjugated, for peak positions below 1725
cm–1, and free, or nonconjugated ones, for positions
above it,[50] shown as diagonally and horizontally
striped bar plots in Figure c, respectively. The results highlight that free carbonyl
groups are particularly more abundant in films formed against solutions
rich in sulfate salts, suggesting that in these films, a larger fraction
of molecules have the carbonyl group connected to a bulkier tail which
could prevent H bonding due to steric hindrance.To test this
hypothesis, we apply a similar analysis to the fingerprint
region, where we integrate all aromatic peaks to estimate the total
concentration of aromatics, and we normalize it by the area of the
(CH2) peak representing
the amount of long alkyl chains. We find that films formed in the
presence of Na2SO4 exhibit the largest amount
of aromatic groups, followed by DI water and chloride salts, as shown
in Figure d. The strong
correlation between aromatic and free acid contents suggests that
the two signals come from the same polar aromatic molecules adsorbed
at the interface. The polar nature of these molecules promotes their
stability at the interface, while their aromatic structure promotes
intermolecular interactions through π–π stacking,
leading to the formation of a complex viscoelastic interfacial skin.
Adsorption Reversibility
The FTIR spectra highlight
that the chemical composition of interfacial films depends on that
of the water phase, which then dictates the mechanical properties
of the oil–water interface. This result suggests that it may
be possible to alter the composition and rheology of the interfacial
films through the aqueous phase chemistry, provided that the adsorption
process is at least partially reversible. This is an important insight
with implications for oil recovery. Indeed, the change in the film
composition could alter its physical properties that in turn could
result in more efficient brine imbibition, oil expulsion, and thus
higher incremental oil recovery.To test the reversibility of
molecular adsorption, we first prepare an interfacial film against
0.1 M NaCl, let it develop over 3 days, and gently replace the water
phase with 0.1 M Na2SO4 solution. In the proximity
of the interface, this salt switch process is slow and driven by diffusion,
such that the interface is only affected by the change in solution
composition and not by the flow applied to replace the water phase.
More details are given in Supporting Information, Section S7. After 3 additional days of equilibration, we collect
the interfacial material and examine its chemical composition through
FTIR analysis. We find that the change in aqueous phase chemistry
entails a change in the composition of the interfacial film, whose
spectrum departs from that of films formed against NaCl solution and
develops features typical of Na2SO4 brine, namely,
a larger aromatic content relative to the long alkyl chains and a
larger amount of free carboxyl groups relative to the bound ones,
as shown by the shift of the C=O peak in Figure a, and quantified in Figure b. The deconvolution details are presented
in Supporting Information, Figure S16.
This result indicates that the adsorption process is indeed partially
reversible and that the composition of a fully developed interfacial
film can be altered by changing the aqueous phase chemistry. More
experiments are required to quantitatively assess the dynamics and
steady state of interfacial film after the solution switch and its
impact on interfacial rheology. This observation can help in understanding
the reported preferential change in wettability in the presence of
sulfate salts.[10]
Figure 4
Adsorption reversibility.
The switch film (NaCl ⇒ Na2SO4) is compared
to the ones formed independently
with NaCl and Na2SO4 salt (all of 0.1 M concentration),
showing the acid region of the FTIR spectra (1500–1900 cm–1) and the fingerprint region (650–950 cm–1). (b) Quantification of relative concentrations of
carboxylic acids (dashed diagonal: bound; dashed horizontal: free)
and aromatics (solid bars) using the areas of deconvoluted peaks.
The salt switch film appears to be a combination of individual salt
films.
Adsorption reversibility.
The switch film (NaCl ⇒ Na2SO4) is compared
to the ones formed independently
with NaCl and Na2SO4 salt (all of 0.1 M concentration),
showing the acid region of the FTIR spectra (1500–1900 cm–1) and the fingerprint region (650–950 cm–1). (b) Quantification of relative concentrations of
carboxylic acids (dashed diagonal: bound; dashed horizontal: free)
and aromatics (solid bars) using the areas of deconvoluted peaks.
The salt switch film appears to be a combination of individual salt
films.
Conclusions
In
this work, we have investigated the formation of interfacial
films between crude oil and aqueous electrolyte solutions, using a
combination of experimental techniques allowing us to probe the time
evolution of interfacial tension, γ, the shear, and extensional
elastic moduli, Gs′ and Es′, and the chemical composition of interfacial
films aged for 24 h. We found that the complex kinetics characterizing
film formation can be simplified by considering the competition between
two classes of surface-active molecules. This competition gives rise
to three distinct phases of film formation. In the earliest stages,
smaller polar molecules adsorb quickly at the interface, causing an
early drop in γ, which depends on the solution composition,
namely on the concentration and valence of the cations in the aqueous
phase. At later times, these small molecules partition to the aqueous
phase and are gradually replaced at the interface by larger molecules,
with polar groups and bulk aromatic systems. These replacements cause
a transient, nonmonotonic evolution of γ, followed by a logarithmic
evolution of both γ and Es′,
independent of the aqueous phase composition. The mechanical properties
of the interface in this regime are dominated by high elasticity (Es′).The latest stage of film formation
is characterized by a deviation
from the simple, logarithmic evolution of γ and Es′ and by the onset of a measurable shear elastic
modulus, Gs′. This onset reveals
that the adsorbed molecules interact with each other, forming a rigid
network with solid-like rheological properties. We find that the onset
of shear elasticity is enhanced in films formed against sulfate-enriched
solutions.The chemical analysis of the fully developed (aged
for 24 h) interfacial
films revealed that films adsorbed on aqueous solutions of Na2SO4 contain a notably larger amount of polar aromatic
compounds. We suggest that these compounds play a pivotal role in
the formation of interfacial elastic films: polar groups help stabilize
the adsorbed molecules at the interface, while the aromatic molecular
body promotes intermolecular π–π interactions favoring
the development of an interconnected molecular network at the interface.Although the adsorption of asphaltenes at crude oil interfaces
is thought to be irreversible, we were able to desorb some of the
components of the developed interfacial network. The observed partial
reversibility of the molecular adsorption upon switching from chloride-
to sulfate-rich solutions confirms the possibility of tuning the physicochemical
properties of the interfacial films. Further studies relating the
chemical composition of films developed with different brines in contact
with reservoir rock minerals and their corresponding surface contact
angles would be needed to provide practical guidelines for oil field
operations regarding wettability alteration to maximize oil recovery.
Authors: Duy Le-Anh; Ashit Rao; Amy Z Stetten; Subhash C Ayirala; Mohammed B Alotaibi; Michel H G Duits; Han Gardeniers; Ali A AlYousef; Frieder Mugele Journal: Micromachines (Basel) Date: 2022-08-14 Impact factor: 3.523