Published at : 10 Jul 2024
Volume : IJtech
Vol 15, No 4 (2024)
DOI : https://doi.org/10.14716/ijtech.v15i4.6736
Olga Soloveva | Institute of Heat Power Engineering, Kazan State Power Engineering University, 420066 Kazan, Russia |
Sergei Solovev | Institute of Digital Technologies and Economics, Kazan State Power Engineering University, 420066 Kazan, Russia |
Rozalina Shakurova | Institute of Heat Power Engineering, Kazan State Power Engineering University, 420066 Kazan, Russia |
Water/oil
(W/O) emulsions are formed during oil fields and production development, thereby
reducing the
oil quality. In
order to separate the
emulsions, specialists use
various methods, equipment, and materials. Most emulsions formed during oil
production are stable and persistent, and traditional methods such
as sedimentation and
centrifugation are ineffective in the separation process. Addressing
this challenge, porous materials characterized by selective super-wetting properties are used for the high-quality
separation of stable W/O emulsions. Therefore, this review
presents recent advancements in
highly porous cellular materials that separate W/O emulsions. It further
discusses the features,
limitations, and advantages of using superhydrophobic/superleophilic and
superhydrophilic/superleophobic porous materials such as metallic and polymeric
foams. The influence of the structure and nature of porous materials on the
efficiency of the separation of W/O emulsions is analyzed. Additionally,
this review also explores
methods for modifying highly porous materials to improve selective wettability.
Absorption capacity; Contact angle; Emulsion separation efficiency; Porous material; Separation of emulsions
Water/oil (W/O) emulsions are a common problem during oil production, formed when water is injected into an oil reservoir to increase pressure and displace oil. Although this method is widely adopted for its high efficiency and ease of implementation, it results in the mixing of W/O leading to the formation of undesired W/O emulsions. These emulsions have an effect on the oil quality, corrode equipment, and pollute water and soil. Subsequently, water, acting as a ballast, introduces specific complications in the transportation and processing of oil, making oil dehydration a mandatory stage in the production process. Therefore, there is a pressing need to study effective methods and materials for separating W/O emulsions (Zeng and Taylor, 2020; Poerwadi et al., 2020). These emulsions are characterized by a two-component system of liquids insoluble in each other, while one phase is continuous, and the second is in a dispersed state. There are three types of emulsions, which include direct type (oil in water), reverse type (water in oil), and complex emulsions (water-oil-water or oil-water-oil) (Camelo-Silva et al., 2022; Jhawat Gulia, and Sharma, 2021). Figure 1 shows the classification and types of emulsions.
Figure 1 Classification and types of emulsions
The main properties of W/O and oil/water (O/W) emulsions
are stability, viscosity, water content, and density (Sapei et
al., 2022). In the various industries,
petroleum/water emulsions exhibit specific characteristics, including oil
density of 0.86–1 (mg/L), emulsions viscosity from 1.40·103 to
9.28·104 (mPa·s), emulsion stability from 0 to 3.36·104
(s), and water content varying between 30–90%. Industrial processes also yield
emulsions based on petroleum products which include diesel O/W (density
0.83–0.85 mg/L, viscosity 8.04·105 mPa·s); fuel O/W (density
0.98–1.00 mg/L, stability from 5.9·102 to 1.3·103 s,
water content 76–77%); gasoline/oil (density 0.71–0.76 mg/L, viscosity 1.5·105
mPa·s) etc. (Fingas and Fieldhouse, 2004). Some of the published studies predominantly
focus on the separation of the processes of
various emulsions such as n-hexane/water (95%, 0.6–0.7 g/cm3, 0.3–0.4 mPa·s) (Qiang et al., 2018), ethanol/water (10–40%, 0.6–0.7 g/cm3,
0.9–2 mPa·s) (Cho et al., 2016), pump O/W (40–80%, 0.85–0.95 g/cm3, 60–80
mPa·s) (Liu et al., 2020), toluene/water (0.85–0.9 g/cm3, 0.5–0.6 mPa·s) (Xu et al., 2021), soybean O/W, etc.
The separation of emulsions includes dividing crude oil into oil and aqueous phases, and this demulsification process is carried out in refineries (Acharya
and Potter, 2021). Various methods
contribute to emulsions separation, including mechanical (Semenov, Slavyanskiy, and Mitroshina, 2021;
Portnov et al., 2021; Solovyev et al., 2021), thermal (Santos et al., 2017; Fortuny
et al., 2007), chemical (Wang
et al., 2021a; Sun et al., 2020; Kang et al., 2006), biological (Zahari, Yan, and Rahim, 2022;
Esmaeili et al., 2021; Fajun et al., 2020; Sachdev and Cameotra, 2013), and electrical (Moldes et
al., 2007; Mostefa and Tir, 2004). Methods such as ultrasound and
magnetic fields are recognized for separating or improving the separation of
emulsions methods. These methods can be effectively combined with highly porous cellular materials for the separation of W/O emulsions.
Porous materials play an active role in
separating W/O emulsions, characterized by
high permeability, low density, hydrophobicity, and lightweight (Satria
and Saleh, 2022; Yang et al., 2021a; Qin et al., 2016). These materials, depending on the types, serve as an effective absorbent or
filter material, intensifying the separation of emulsions in the
implementation of thermal separation methods (Wu et
al., 2020a; Yan et al., 2020; Yang et al., 2019). Figure 2 shows diagrams of the process of separating O/W emulsions using porous material, which is used as an absorbent (Figure 2a) or as a filter material (Figure 2b).
Numerous publications focus on the use of porous materials for the
separation of W/O emulsions. Many investigations have solved problems such as the
separation of W/O emulsions using metal (Solov’eva et al., 2021) and polymer (Qiang et al., 2018) foams, studied the adsorption capacity and efficiency of emulsions
separation by hydrophobic (Xue et al., 2021a) and hydrophilic materials, examined the methods for applying a
hydrophobic coating to the surface of porous material (Álvarez-Gil,
Ramirez, and Fernandez-Morales, 2021), synthesized the composite porous materials by surface modification (Cho
et al., 2016),
assessing the influence of the type of modifier and the concentration on water
contact angle (WCA), adsorption capacity, and emulsions separation efficiency (Ahmed, Anis, and Khalil, 2021; Zhang,
Liu, and Qiao, 2020). Investigations also examine factors such as the influence of liquid pH
on adsorption capacity (Alazab and Saleh, 2022). Researchers have studied the
features of emulsion separation using materials such as polyurethane foam,
melamine foam, polydimethylsiloxane foam, nanocellulose sponge, iron foam,
nickel foam, and copper foam. Various surface modifiers (metal nanoparticles,
polymer compounds, carbon nanotubes) and methods of their application
(immersion in solution, polymerization, freeze-drying, sol-gel process, etc.)
have been studied. In addressing these aspects, scientists have solved many
problems related to the separation of W/O emulsions by porous media.
The purpose of this study is to systematize and
classify research results, as well as to identify unsolved problems in this
area. The relevance and novelty of this review lie in providing comprehensive
systematic data on research related to the separation of emulsions. This
information assists specialists by helping in the identification of (i) the
effective use of porous materials to separate certain types of emulsions, and
(ii) synthesizing composite porous materials with the necessary properties to
solve specific engineering problems. In this review, articles focusing on
emulsion separation using metal and polymer porous materials were selected. The
data were classified according to the material of the porous medium (metal,
polymer); wettability of the material (hydrophobic, oleophobic); type of
modifier; method of applying the modifier to the surface of the porous medium;
the influence of the modifier on the properties of porous medium (contact
angle, adsorption capacity).
This systematic
review specifically focuses on metal and polymer porous materials used for
separating emulsions, namely foams made from nickel, iron, polyurethane,
melamine, polydimethylsiloxane, etc. This review discusses two methods for
separating emulsions: filtration and adsorption, which are implemented using
porous materials. Furthermore, the distinctive feature and advantage is the
analysis of the influence of various surface modifiers (metal nanoparticles,
polymer compounds, graphene, etc.) on surface wettability and emulsion
separation characteristics (separation efficiency and adsorption capacity).
Figure 2 Separation
of O/W emulsions using porous materials by adsorption (a) and filtration (b)
Surface
wettability is the fundamental characteristic of materials for emulsion
separation (Wang and Deng, 2019). It is
assessed by measuring WCA.
2.1. Water contact
angle (WCA) in
air
Theoretically,
WCA depends on the interaction between the solid, liquid, and gaseous phases
for a perfectly smooth surface. WCA can be obtained from Young’s
Equation (1) (Jiang, Müller-Plathe, and Panagiotopoulos, 2017):
where – contact angle on a perfectly smooth surface, surface tension between a solid and a liquid solid and gas and liquid and gas surface is considered hydrophilic, at >90° hydrophobic, and a surface with contact angle >150° is called superhydrophobic (Yang et al., 2021b) (Figure 3).
Young's equation describes the wettability of a perfectly smooth surface, however, the real surface is rough. According to the study by Robert Wenzel, it was reported that water droplets fill the rough structure, thereby increasing the contact area and surface wettability, in which case Equation (2) applies (Sarkar and Kietzig, 2013):
where W – apparent
contact angle, r – the ratio of the contact area of the interface between a
solid and a liquid in the case of a rough surface to the contact area in the
case of a perfectly smooth surface. Applying equation (2) to surfaces with high
roughness or to porous structures, the value of cosW will be
greater or less than one, which is unacceptable from a mathematical point of
view. In the Cassie-Baxter theory, air pockets under a layer of water are
considered a superhydrophobic environment, which prevents water penetration (Chu,
Feng, and Seeger, 2015). The Cassie-Baxter regime is described by the following contact angle
Equation (3) (Feng and Jiang, 2006):
Figure 3 WCA formed by liquid droplets on a smooth,
solid surface, in the air.
2.2. Contact angle under water or oil
The above wetting regimes are
valid for the case of liquid contact with a solid (smooth or rough) surface in
the air. However, to calculate the contact angle of liquid drop A (LA)
under liquid B (LB) the following Equation (4) is derived (Liu
et al., 2009):
where – surface tensions at the interfaces, respectively: liquid A-gas, liquid B-gas,
and liquid A-liquid B. The angles A and B are the contact
angles of fluids A and B with air. Figure 4 shows the modes of surface wetting
with liquid A under liquid B.
Depending on the contact angle, the wettability regime, and the environment (air, water, oil), there are several possible extreme wettability states (Wang et al., 2015; Chen and Xu, 2013), namely: superhydrophilic, superhydrophobic, superolephilic, and superoleophobic wettability in the air; underwater superoleophobicity and underwater superoleophilicity in water; underoil superhydrophilicity and underoil superhydrophobicity (Li et al., 2016a; Wang et al., 2015).
Figure 4 Regimes of wetting a solid surface with
liquid A (LA) in liquid B (LB)
To describe the properties of porous materials used for emulsion separation and evaluate their effectiveness, the comparison includes characteristics such as contact angle, absorption capacity, and emulsion separation efficiency. We consider surfaces with WCA of 0°, 90°, >90° and >150° to be superhydrophilic, hydrophilic, hydrophobic, and superhydrophobic, respectively. Surfaces with oil contact angles (OCA) of 0°, 90°, >90° and >150° we consider to be superoleophilic, oleophilic, oleophobic and superoleophobic, respectively.
Absorption capacity is determined
by immersing the test material in W/O until the material is saturated with
liquid. The test sample is then removed from the liquid, and the mass is
measured. Absorption capacity (Q) is calculated by Equation (5) (Meng
et al., 2017):
where ms and ms,o – the
mass of the test material before and after liquid absorption, respectively.
Absorption capacity is measured in g/g, and the process is influenced by
factors such as porosity and pore size of the adsorbent; pH, density, and
viscosity of a liquid; size of liquid molecules; concentration of dispersed
phase particles (SobolCiak et al., 2021). The wetting regime is
influenced by the porosity and pore size of the adsorbent. As these increase,
the liquid penetration into the porous structure also increases. Porous
materials absorb high-viscosity liquids, such as oil or diesel, better than
low-viscosity liquids, such as hexane, that is, the adsorption capacity is
proportional to the density of the oil (Wang et
al., 2020; Li et al., 2019a). The adsorption capacity of porous material to
droplets of oil in the emulsion varies depending on the pH of the water.
According to a study by (Alazab and Saleh, 2022), the highest adsorption capacity
was achieved in neutral water (31 g/g at pH = 7); in an acidic environment, the
adsorption capacity decreased slightly (30 g/g at pH = 2), in an alkaline
environment, porous material absorbs oil even worse (26 g/g at pH=12).
According to (Ahmed, Anis, and Khalil, 2021), the smaller the size of oil droplets, the
lower the adsorption capacity.
The emulsion separation
efficiency is calculated by Equation (6) (Li et al., 2019b):
where Cfeed – oil concentration in
the initial emulsion, Cfiltrate – oil concentration in the filtrate.
3.1. Metal Foams Used
for Emulsion Separation
Porous metals are actively used in industry to solve various problems
related to filtration and heat transfer (Solovev et al., 2022; Soloveva et al., 2022; Soloveva, Solovev, and Yafizov, 2021; Solovev et al., 2019). These metal foams exhibit
effective absorption of both water and oil well. Therefore, to separate W/O emulsions, hydrophobic coating, for example, HDTMS, hydrophobic silica,
carbon nanoparticles, etc., is applied to the surface of the metal foam. For
instance, the study by (Zhang et al., 2019a) developed nickel foam by
synthesizing the ZnO@Co3O4 hierarchical structure using
hydrothermal method followed by calcination and hydrophobic modification with
HDTMS. The modified foam showed a high WCA of 158°, separation efficiency
varied from 97 to 99%. The following methods are used for coating the surface of metal foam:
electrochemical deposition method (Zhang et al., 2023), immersion deposition method (Eum
et al., 2019),
simple dipping method followed by drying in an oven (Wang et
al., 2021b),
acid dipping and etching method (Álvarez-Gil, Ramirez, and
Fernandez-Morales, 2021), etc. In the study by (Zhang
et al., 2019b) hydrophobic-oleophilic iron foam
was developed by immersion in n-dodecyl mercaptan (NDM). The Fe-NDM foam showed
high hydrophobicity (WCA=145°) and a separation efficiency of O/W emulsions of 98%. Subsequently, coating a metal
foam results in a reduction in cell size and a decrease in the permeability of
the foam. The coating should be as thin as possible while providing high hydrophobic
or oleophobic properties. In the study, (Chen et
al., 2020) proposed a method for applying a superoleophobic
coating, in which a metal felt was immersed in a colloidal suspension of
silicon dioxide, washed, dried, and then annealed at 550°C. The thickness of
the coating layer was about a hundred nanometers, thereby the pore sizes
remained practically unchanged. The resulting material showed high efficiency
in absorbing water from W/O emulsions, maintaining excellent
performance after 30 use cycles.
Metal foams have been extensively examined as an absorbent material for
separating W/O and O/W emulsions. However, using porous
metals as coalescing baffles in gravity-dynamic separators is also known from
the literature. A comparison between plate and highly porous partitions serves
to intensify the process of separation of the emulsion. In a study by (Solov’eva et al., 2021), the influence of the baffle
design on the emulsion separation process was investigated. A comparison
between the plate and highly porous baffles showed that porous baffles provide
more effective separation at low emulsion flow rates, and plate baffles are
more effective at high emulsion flow rates.
Metal foams are characterized by the following advantages, which include high mechanical strength and lightweight, high porosity, and large surface area. However, the widespread application is affected by susceptibility to contamination and corrosion. In emulsion separation, the foam becomes clogged with oil droplets and organic substances, which leads to a decrease in the wettability of the surface and a decrease in separation efficiency. The foam must be washed periodically, for example, with ethanol, to restore the performance. To solve the problem of pollution, scientists are developing foams capable of self-cleaning (Li et al., 2022; Wu et al., 2020b; Kang et al., 2018). Self-cleaning surfaces are characterized by a high static WCA and a small sliding angle, which leads to the so-called self-cleaning effect (Zhang et al., 2013). Another disadvantage of metal foams is corrosion, and hydrophobic and anticorrosive coating is often applied to the surface of the foam to solve this problem (Li et al., 2022).
3.2. Polymer foams used for emulsion separation
In addition to metal foams, polymeric foams are used to separate
emulsions. The most widely used polyurethane (PUF) and melamine foams (MF) are
due to their cost-effectiveness, ease of production, and high wettability.
Polymeric foams are characterized by high hydrophilicity and oleophilicity (Krishnamoorthi et al.,
2021; Wang et al., 2014). Foams are often coated with hydrophobic/oleophilic, less often with
hydrophilic/oleophobic coating to separate emulsions (Jin et
al., 2022; Li et al.,
2018; Li et al.,
2016b). Hydrophobic
coatings increase surface roughness (Hou et al., 2019), thereby ensuring hydrophobicity
of the material (Ejeta et al., 2021). Table 1 shows the
characteristics of polymeric foams modified with various hydrophobic coatings.
Surface modifier affects the adsorption capacity
of porous material. In a study by (Qiang et al., 2018), they synthesized
composite sponges based on polyurethane foam and graphene oxide nanoribbons
(GONR) and modified them with two different silanol groups:
trimethoxyoctadecylsilane (TMOS) and trimethoxysilane (FAS). TMOS-modified foam
became superhydrophobic (WCA=153°) and superoleophilic (OCA = 0°). The foam
treated with FAS achieved superhydrophobicity using WCA of 165 contact angle
with superoleophobic behavior towards specific oils such as diesel, toluene,
and n-hexane. Surface modification influenced the foam adsorption capacity,
with FAS-modified samples showing significantly lower absorption rates for
n-hexane, toluene, gasoline, and diesel compared to samples treated with GONR
and TMOS. The study reported that the surface properties of composites could be
adapted to water or oil by adjusting the end groups of silane molecules.
Hydrophobic coating changes the surface roughness of the foam, forms a
hierarchical structure, and leads to an increase in capillary forces, which
affects the rate of oil adsorption. In a study by (Xue et
al., 2021b)
PU foam was modified with polydimethylsiloxane (PDMS/PU) and copper
terephthalate (CuT-PA/PDMS/PU). CuTPA/PDMS/PU foam had higher roughness than
PDMS/PU foam, and the presence of a hierarchical structure resulted in increased
capillary forces and an 8-fold increase in motor oil adsorption rate compared
with PDMS/PU foam. In another study by (Xu et al., 2021) MF was modified with microporous polymers using
carboxyl (CMP-COOH) and hydroxyl (CMP-OH) groups. Modification with carboxyl
groups provides a higher adsorption capacity of the composite foam, for
comparison: the adsorption capacity of CMP-COOH and CMP-OH foams for toluene
was 75 g/g and 56 g/g, respectively. The modifier concentration also affects
the adsorption capacity. According to the study by (Xue et
al., 2021a)
melamine sponge was modified with MXene and tetradecylamine (TDA) in
different concentrations. Increasing the concentration of both MXene and TDA
increased WCA. The addition of MXene increased oil adsorption capacity compared
to pure melamine sponge.
However, MXene@MS foam continued to absorb water
due to its hydrophilic nature. The addition of TDA reduced the surface energy
of the melamine sponge, increasing hydrophobicity. As a result, TDA@MS and
TDA-MXene@MS composite foams did not absorb water at all and displayed higher
oil adsorption capacity. This indicates that the choice of modifier and its
concentration influence surface roughness, form a microporous hierarchical
structure, bolster capillary forces, and consequently impact oil adsorption
capacity and rate.
In addition to the above modifiers, polymer
foams are modified with reduced graphene oxide (Jamsaz and
Goharshadi, 2020; Zhang, Liu, and Qiao, 2020; Zhou et al., 2019; Cao et al., 2019; Zhang et al., 2017), carbon
nanotubes (Visco et al., 2021), carbon nanofibers (Guo
et al., 2021; Baig,
Alghunaimi, and Saleh, 2019),
carbon black (Chen et
al., 2023; Yang et
al., 2023), etc. Carbon modifiers contributed to a
significant increase in the hydrophobicity of foams (WCA > 150°), and also
improved the mechanical properties.
In addition to polyurethane foam and melamine
foam, less common polymeric foams are known to be synthesized from
polystyrene-divinylbenzene (Zhang et al., 2016),
polylactic acid (Wang et al., 2019), and
polypropylene (Mi et al., 2019).
Traditionally, emulsion separation materials
have been characterized by either hydrophobic or oleophobic properties.
However, contemporary investigation is focusing on developing materials with
opposite wettability, capable of displaying both hydrophobic and oleophobic
properties, depending on the conditions. For example, when the material is
pre-wetted with oil, it exhibits superoleophilic and superhydrophobic
properties. Conversely, when the material is initially wetted with water, it
shows superhydrophilic and superleophobic properties. This behavior is
explained by the presence of hierarchical voids in the material. If the
material has micro- and nano-sized pores, the first infusion liquid, for
example, water, penetrates through the micropores. Laplace forces retain the
second (oil), and the material exhibits superleophobic properties.
Despite the extensive
investigations in using porous materials for separating emulsions, critical
challenges persist including (i) protecting metal porous adsorbers from corrosion
and (ii) cleaning adsorbers from oil contaminants to extend the service life
remain unresolved.
Table 1 Characteristics of polymeric
foams modified with hydrophobic coatings
Base material |
Coating material |
WCA |
Oil |
Oil absorption capacity,
g/g |
Ref. |
PUF |
Graphene oxide
nanoribbons |
153° |
n-hexane |
34 |
(Qiang et al.,
2018) |
Stearic acid |
140° |
n-hexane |
23 |
(Wang and Zheng,
2017) | |
Octadecyl
Trichlorosilane |
156° |
n-hexane |
21 |
(Liang et al.,
2019) | |
Fe3O4
nanoparticles, |
145° |
n-hexane |
10 |
(Alazab and Saleh, 2022) | |
Titanate nanotubes |
128° |
n-hexane |
20 |
(Pan et al.,
2015) | |
Polydimethylsiloxane |
157° |
n-hexane |
12.5 |
(Xue et al.,
2021b) | |
MF |
Microcrystals MgAl-LDH |
163.2° |
n-hexane |
70.5 |
(He et al.,
2022) |
TiO2
nanoparticles |
161.1° |
ethanol |
46 |
(Cho et al.,
2016) | |
Polydimethylsiloxane |
157° |
ethanol |
58 |
(Wang et al.,
2020) | |
Copper nanoparticle |
148.5° |
pump oil |
90 |
(Li et al.,
2019c) | |
Waste epoxy resins |
146.5° |
pump oil |
80 |
(Liu et al.,
2020) | |
Conjugated microporous
polymers |
153.92° |
toluene |
73 |
(Xu et al.,
2021) | |
Acrylic copolymer/silica |
153.5° |
n-hexane |
78 |
(Li et al.,
2019b) | |
Tetradecylamine-MXene |
152° |
toluene |
60 |
(Xue et al.,
2021a) | |
Halloysite NP and
SiO2 |
158° |
toluene |
110 |
(Song et al.,
2022) | |
PDMS foam |
Graphene |
130.8° |
n-hexane |
10.2 |
(Pan et al.,
2021) |
Multiwalled carbon
nanotubes |
157° |
– |
– |
(Zhou et al.,
2023) |
In conclusion, porous materials with selective wettability were actively used to separate O/W and W/O emulsions formed during oil production or as a result of oil spillage. At industrial enterprises, various emulsions were formed, the properties of which depend on the density (0.71 – 1.07 g/mL) and viscosity (from 1 to 3.04·105 mPa·s) of petroleum and oil, as well as water content (10 – 90%). To improve the oil quality and purify wastewater, O/W, and W/O emulsions were separated by adsorption or filtration with porous materials. This review systematically presented the results of the separation of emulsions by porous media, emphasizing the influence of surface modifiers on the separation characteristics. The analysis showed that the type and concentration of the modifier significantly influenced WCA, adsorption capacity, and separation efficiency. The water contact angle (WCA) of PU foam, treated with different hydrophobic coatings, ranged between 1280 and 1570, showcasing hydrophobicity or superhydrophobicity. Additionally, the adsorption capacity for n-hexane fluctuated from 10 to 34 g/g. The viscosity and density of emulsions also affected adsorption capacity. Porous materials absorb high-viscosity liquids (2·103 – 2·105 mPa·s) better than low-viscosity liquids (0.5 – 120 mPa·s). Hydrophobic and oleophilic composites were used for the adsorption of oil from emulsions. Accordingly, these composites are advisable to use for eliminating oil and oil products that spill water. Hydrophobic composites were not suitable for gravitational separation of emulsions, because water naturally settles under oil on the surface of the composite, forming a barrier layer and preventing oil droplets from penetrating the pores. In addition, hydrophobic composites quickly become contaminated with oil during gravitational separation. In this scenario, it was advisable to use hydrophilic and oleophobic porous composites.
This review was funded by the Russian Science
Foundation, Grant Number 21-79-10406, https://rscf.ru/en/project/21-79-10406/.
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