SlideShare a Scribd company logo
1 of 10
Download to read offline
See discussions, stats, and author profiles for this publication at: https://www.researchgate.net/publication/51158161
New Pickering Emulsions Stabilized by Bacterial Cellulose Nanocrystals
ArticleĀ Ā inĀ Ā Langmuir Ā· June 2011
DOI: 10.1021/la200971fĀ Ā·Ā Source: PubMed
CITATIONS
529
READS
2,128
4 authors, including:
Some of the authors of this publication are also working on these related projects:
innovation management and sustainability - Safer-by-Design View project
Modelling and assessment of a small scale flexible biorefinery in urban and peri-urban areas in Nantes and Hamburg. View project
Irina Kalashnikova
23 PUBLICATIONSĀ Ā Ā 1,670 CITATIONSĀ Ā Ā 
SEE PROFILE
Bernard Cathala
French National Institute for Agriculture, Food, and Environment (INRAE)
146 PUBLICATIONSĀ Ā Ā 5,426 CITATIONSĀ Ā Ā 
SEE PROFILE
Isabelle Capron
French National Institute for Agriculture, Food, and Environment (INRAE)
74 PUBLICATIONSĀ Ā Ā 4,023 CITATIONSĀ Ā Ā 
SEE PROFILE
All content following this page was uploaded by Irina Kalashnikova on 20 December 2017.
The user has requested enhancement of the downloaded file.
Published: May 23, 2011
r 2011 American Chemical Society 7471 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
ARTICLE
pubs.acs.org/Langmuir
New Pickering Emulsions Stabilized by Bacterial
Cellulose Nanocrystals
Irina Kalashnikova, Herv
e Bizot, Bernard Cathala, and Isabelle Capron*
UR 1268 Biopolym
eres, Interactions et Assemblages, INRA, F-44316 Nantes, France
b
S Supporting Information
1. INTRODUCTION
An emulsion is a system of dispersed droplets of one im-
miscible liquid in another stabilized by emulsiļ¬ers. Since the
pioneering work of Ramsden1
and Pickering,2
solid colloidal
particles have been shown to adsorb at ļ¬‚uid interfaces to form
so-called ā€œPickering emulsionsā€. The properties of these systems
are due in part to the irreversible nature of such particle
adsorption.35
Interest in Pickering emulsions has been renewed
over the past 10 years, especially for health and cosmetics
applications where the use of surfactants is undesirable. Indeed,
they not only present good mechanical properties, but much
fewer particles are required to produce good stability, thereby
leading to a reduction in the use of hazardous surfactants and
their environmental consequences.6,7
Stabilization of solid particles at the interface is generally
considered to be directed by particle wettability, which is itself
directed by the more or less hydrophilic/hydrophobic nature of
the surface. The formation of an oil in water (o/w) emulsion will
occur for hydrophilic surfaces. On the opposite, a stable water-in-
oil (w/o) emulsion will be produced for hydrophobic surfaces.8
If the particles are completely wetted by water or oil, they may
remain dispersed in either phase and no stable emulsion will
form.9
Most of the literature dealing with Pickering stabilization
concerns various types of inorganic, commercially available
particles such as silica,4,1012
montmorillonite,13
Laponite,14
calcium carbonate,3,15
carbon graphite,3
or various latexes.4,16
However the raw, non-surface-treated nanoparticles are usually
not surface active due to their lack of hydrophilicity/hydropho-
bicity, or great tendency to aggregate. Methods involving surface
modiļ¬cations6
or the addition of cosurfacting compounds17,18
have been developed to produce symmetrical or asymmetrical
(Janus) particles, but such methods increase the use of chemicals
and make the process complicated for large-scale production.
Research eļ¬€orts are being focused on the development of
environmentally friendly, biobased nanocomposites, but few
studies, up to now, have described stabilization by particles
derived from renewable resources.1921
Cellulose is one of the
most widespread biopolymers and is a good candidate because of
its sustainability, biodegradability, and nontoxicity.
Cellulose is a linear homopolymer of Ī²(1-4)-D-glucose resi-
dues linked together by glycosidic oxygen bridges. It exists in
nature as highly resistant ļ¬bers. The high cohesive energy is
induced by van der Waals forces and by extensive hydrogen bond
networks within and between the chains via the hydroxyl groups
in equatorial position.22
These ļ¬bers are formed by the stacking
of microļ¬brils, and it is now recognized that the ordered crystal-
line regions are interrupted by amorphous or less ordered regions
along the elementary ļ¬bril where the microļ¬brils are distorted by
internal strain.23,24
A few investigations have used cellulose derivatives such as
microļ¬brillated cellulose (MFC), which are moderately de-
graded microļ¬brils (510 Ī¼m long), to stabilize oil in water
emulsions,19,25
but their long length compared to the size of
the droplets produced networks rather than individual drops.
In order to control the emulsion characteristics, the particle size
must be reduced. Concerning interfacial stabilization, most of
the studies have been carried out on hydrophobically modiļ¬ed
cellulosic material26
leading to water in oil emulsions. They
Received: March 15, 2011
Revised: May 9, 2011
ABSTRACT: We studied oil in water Pickering emulsions stabilized
by cellulose nanocrystals obtained by hydrochloric acid hydrolysis of
bacterial cellulose. The resulting solid particles, called bacterial cellu-
lose nanocrystals (BCNs), present an elongated shape and low surface
charge density, forming a colloidal suspension in water. The BCNs
produced proved to stabilize the hexadecane/water interface, promot-
ing monodispersed oil in water droplets around 4 Ī¼m in diameter
stable for several months. We characterized the emulsion and visua-
lized the particles at the surface of the droplets by scanning electron microscopy (SEM) and calculated the droplet coverage by
varying the BCN concentration in the aqueous phase. A 60% coverage limit has been deļ¬ned, above which very stable, deformable
droplets are obtained. The high stability of the more covered droplets was attributed to the particle irreversible adsorption associated
with the formation of a 2D network. Due to the sustainability and low environmental impact of cellulose, the BCN based emulsions
open opportunities for the development of environmentally friendly new materials.
7472 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
involved acetylated nanoļ¬bers,27,20
sililated microļ¬brils,28
or carboxymethylated cellulose,29
but none reported the
production of stable oil in water droplets. It has been known
for many years that stable nanoparticle suspensions can be
prepared by treating native cellulose to harsh acid
hydrolysis.30,31
Acid hydrolysis is a heterogeneous process
which involves ļ¬rst the diļ¬€usion of acid into the ļ¬bers followed
by the cleavage of the glycosidic bonds, resulting in a turbid
colloidal suspension. Sulfuric acid is commonly used in introdu-
cing sulfated charges at the surface. The absence of charge
generally leads to the production of crystalline aggregates.32
In
the literature, these crystallites are referred to as whiskers or
nanocrystalline cellulose.
In this work, cellulose nanoparticles were prepared via hydro-
chloric acid hydrolysis of bacterial cellulose. The bacterial
cellulose was chosen on its availability since it can be easily
produced from nata de coco, in which cellulose is present at
rather high concentration. Moreover, it is possible to get it wet,
whereas most of the other sources available provide dry material
and present limited contaminants, that is, without any hemi-
cellulose or various byproduct generally surrounding cellulose.
It is then possible to hydrolyze it with milder conditions and,
notably, to avoid the use of sulfuric acid which promotes highly
charged surfaces. Finally, characteristic features of bacterial
cellulose nanocrystals (BCNs) are their large aspect ratios and
ļ¬‚at, ribbonlike cross sections. As a result, pure low charged BCNs
were used, without further desulfation, modiļ¬cation, or addition
of any cosurfacting product, to stabilize the interface of an oil
in water emulsion. These BCNs were characterized, and the
stability of the emulsion, drop size, and coverage characteristics
were investigated.
2. MATERIALS AND METHODS
2.1. Materials. Nata de coco was a gift from Mrs. Joann Dar, who
bought it in San Jose (Central Luzon, Philippines) from a traditional
producer. All other products were purchased at 99% or greater purity.
n-Hexadecane (Sigma) was cleaned thoroughly with water to remove
any remaining surfactants. Styrene (Fluka) was purified: tert-butylcate-
chol inhibitor was removed by percolation through a cartridge filled with
activated alumina (EcoChrom N super1) regenerated by treatment at
400 Ā°C. Polymerization was initiated with V65 (2,20
-azobis(2,4-dimethyl
valeronitrile)) which was a gift from Qingdao Runxing Photoelectric
Material Co. (LTD, Qingdao, China). For CLSM BODIPY (4,4-
difluoro-4-bora-3a,4a-diaza-s-indacene) (Molecular Probes Invitrogen,
Eugene, OR) and calcofluor (Sigma) were used without purification.
2.2. BCN Preparation. BCNs were obtained from nata de coco
cubes ground in a Waring blender at maximum speed. The resulting
slurry was filtered and resuspended in 0.5 N NaOH and then stirred in a
lidded flask for 2 h at 70 Ā°C. Alkali was removed by rinsing with distilled
water to neutrality. After that, bleaching treatment was performed twice
by mixing the suspension with a 8.5 g/L NaClO2 solution in sodium
acetate buffer (pH 4.5) at 70 Ā°C for 2 h. The bleached cellulose was
rinsed with distilled water until the pH remained stable.
The puriļ¬ed bacterial cellulose was then hydrolyzed with 2.5 M HCl
at 70 Ā°C for 2 h as described by Gilkes et al.33
Acid was removed by
successive centrifugations during 10 min at 10 000g and redispersion of
the solid materials in ultrapure water (18.2 MĪ©) up to pH  5. The
suspension was further homogenized by ultrasound treatment for about
1 min (ultrasonic processor XL 2020, Misonix, Farmingdale, NY). The
resulting 1% suspension was then extensively dialyzed against water
to remove any remaining contaminants and deionized by mixing with
mixed bed ion-exchange resin. For storage, one drop of CHCl3 per
250 mL was added to the suspension and kept at 4 Ā°C.
2.3. Transmission Electron Microscopy (TEM). A total of
20 Ī¼L of a BCN suspension in water (0.1% w/v) was deposited on a
freshly glow-discharged carbon-coated electron microscope grid (200
mesh copper, Delta Microscopies, France) and the excess removed.
Negative staining was performed by adding 20 Ī¼L of uranyl acetate
solution (2% w/v). The excess solution was removed and the grids were
dried in an oven at 40 Ā°C just before observation. The grid was observed
under standard conditions with a JEOL JEM-1230 transmission electron
microscope operating at 80 kV.
2.4. Emulsion Preparation and Characterization. Emulsion
Preparation. The oil in water (o/w) emulsions were prepared using
hexadecane and a BCN aqueous suspension at the required concentra-
tion without further dilution. All the emulsions were prepared using an
oil/aqueous phase ratio of 30/70. Practically, 0.3 mL of hexadecane was
added to 0.7 mL of aqueous suspension in a plastic vial and sonicated
with an ultrasonic device with a dipping titanium probe close to the
surface (power level at 1.5 dial value corresponds to 2 W/mL applied
power determined by heat balance), alternating 3 s sonication with a 3 s
standby for 20 s.
Stability Test. Stability of the generated emulsions was checked by
centrifugation for 2 min at 4000g. The emulsion volume and drop
size measured for various centrifugation times kept stable from 30 s to
40 min. Photographs of the vials containing the emulsions were taken
with a P1 digital camera (Olympus), and the thickness of the creaming
layer was measured with a digital caliper.
Light Microscopy. The emulsions were all visualized by light micro-
scopy. A total of 15 Ī¼L of the resulting Pickering emulsion was added to
1 mL of distilled water and stirred by vortex, then a single drop was
poured onto a slide and observed via microscope (BX51 Olympus).
Droplet diameter was measured by image analysis using the ā€œImageJā€
software and compared to the drop size distribution determined by laser
light diffraction using a Malvern 2000 granulometer apparatus equipped
with a HeNe laser (Malvern Instruments, U.K.) with Fraunhofer
diffraction. The measurements were systematically carried out in tripli-
cate. The diameter was expressed as surface mean diameter D(3,2) (the
Sauter diameter), and eventual aggregation was checked by comparing
these values with those where sodium dodecyl sulfate (SDS) was added
just before measurement. Similar results were obtained via granulometer
and ImageJ analysis.
Sugar Analysis. In order to evaluate the amount of cellulose involved
in the droplet stabilization, quantification of the cellulose released in the
aqueous subphase after centrifugation was carried out by colorimetric
titration after sulfuric acid degradation. Subphases were lyophilized,
dispersed in 26 N sulfuric acid for 1 h at 25 Ā°C, and afterward hydrolyzed
in 2 M sulfuric acid for 6 h at 100 Ā°C before colorimetric titration with
orcinol sulfuric acid method with a Skalar autoanalyser. Glucose was
used as a standard.
2.5. Confocal Laser Scanning Microscopy (CLSM). For
CLSM visualization, the emulsions were prepared with double staining.
Hexadecane and cellulose were stained with BODIPY (564/570)
fluorophore andcalcofluor (347/450) respectively. Images were acquired
using a Zeiss LSM 410 confocal microscope (Zeiss, Gottingen, Germany)
using a x40 water-immersion lens with an optical section thickness
around 2 Ī¼m.
2.6. Scanning Electron Microscopy (SEM). Because of hex-
adecane volatility, the emulsions formed could not be introduced in
the SEM chamber. The BCNs proved to stabilize the styrene/water
interface and form a stable emulsion. This ability to form solid particles
was then used to visualize the distribution of BCNs at the drop inter-
face by SEM. Therefore, aqueous suspensions containing 0.5, 1, and
5 g/L BCNs were sonicated for 20 s and degassed with nitrogen for
10 min. Styrene was mixed with V65, an oil-soluble initiator, to obtain a
7473 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
styrene/V-65 ratio of 120/1 (w/w).14
A total of 86 Ī¼L of this mixture
was added to 1.0 mL of the BCN suspension, and an emulsion was
prepared by sonication for 20 s (3 s pulse on, alternating with 3 s pulse
off). Then 500 Ī¼L of water was added to dilute the already formed
Pickering droplets. After vortex mixing, the emulsions were again
degassed with nitrogen gas for 10 min before polymerization at 63 Ā°C,
without stirring, for 24 h. The dried beads were metallized with platinum
and visualized with a JEOL 6400F instrument.
2.7. Coverage Determination. Coverage was determined from
the amount of particles involved in the emulsion and the oil effectively
trapped within the droplets. The absence of BCN in the nonemulsified
aqueous phase after centrifugation was confirmed by sugar analysis
after sulfuric hydrolysis. The surface coverage C is then given by the ratio
of the theoretical maximum surface susceptible to be covered by the
particles Sp and the total surface displayed by the oil droplets Sd:
C Ā¼
Sp
Sd
ư1ƞ
where
Sp Ā¼ NpLl Ā¼
mp
hFp
ư2ƞ
and
Sd Ā¼ 4Ļ€R2 3Voil
4Ļ€R3
Ā¼
3Voil
R
ư3ƞ
where Np is the number of BCNs, L, l. and h are, respectively, the length,
width, and thickness of BCN, mp is the mass of BCNs, Fp is the BCN
density, R is the average drop radius, and Voil the volume of oil included
in the emulsion after centrifugation.
The total coverage can be expressed as
C Ā¼
mpD
6hFVoil
ư4ƞ
where D is the D(3,2) average radius of the droplets.
3. RESULTS AND DISCUSSION
3.1. BCN Preparation. BCNs were isolated by acid hydrolysis
to remove the amorphous part of the microfibrils and then
dispersed using a sonication device. Bacterial cellulose hydrolysis
is generally performed with sulfuric acid which leads to charged
particles,34
whereas hydrolysis with hydrochloric acid results in
slightly carboxylated surfaces.35
The nanocrystals generated by
sulfuric or hydrochloric hydrolysis have rectangular cross sec-
tions or a ribbonlike shape with dimensions of ca. 10 nm  50 nm
and range in length from 100 nm to several micrometers, with
these dimensions depending on the hydrolysis conditions.34,36
The bacterial cellulose used in this work was hydrolyzed with
hydrochloric acid. At the end of the process, the sample charge
density was measured by conductometric titration (see the
Supporting Information). This titration revealed a low level of
residual charges, involving weak charge groups such as carboxylic
groups, below 103
e/nm2
. TEM images of the suspension
showed that the crystalline particles were fairly homogeneous,
despite a tendency to aggregate due to the absence of repulsive
surface charges (Figure 1). This aggregation is not observed with
sulfated cellulosic nanoparticles such as cotton whiskers.31
Analysis of the TEM images using ImageJ software indicated
an average length of 855 nm and width of 17 nm. A thickness
of 7 nm was determined by atomic force microscopy (AFM)
(see the Supporting Information). These data are in accordance
with most other authors who reported sizes for the individual
nanocrystals from bacterial cellulose thickness ca. 510 nm and
length from 100 to 1000 nm for acid-treated samples37,38
whereas the reported width ranged from 5 to 50 nm.35,37
As a
result, the particles produced show crystalline, elongated, sub-
micrometer sized characteristics.
3.2. Emulsion Preparation. The aqueous phase, for all tested
emulsions, consisted of cellulosic nanocrystalline particles dis-
persed in water at the required concentration without further
treatment. Hexadecane was added afterward. The biphasic
system was then sonicated, resulting in a very stable oil in water
emulsion.
Respective localization of the nanocrystals at the oil interface
and ordering of the dropletā€™s surface was checked by CLSM and
SEM. Calcoļ¬‚uor was used as ļ¬‚uorochrome for cellulosic materi-
al, while BODIPY presenting aļ¬ƒnity for hydrophobic liquids was
dissolved in the oil phase. This double staining allows one to
clearly distinguish the inner oily phase and the surface covered by
cellulosic particles (Figure 2a). Surface organization was exam-
ined in detail by SEM visualization of the individual droplets.
Although cryo SEM would allow direct observation of oil in water
Pickering emulsions,39
polymerizable resins oļ¬€er convenient
alternatives for oil in water emulsion using the classical SEM
approach. Bon and Colver prepared latex particles using Lapo-
nite clay discs as stabilizers, with the inner part being polymerized
from a variety of hydrophobic monomers.14
BCNs showed the
same ability to stabilize styrene and hexadecane droplets, and
therefore, styrene was selected. An aqueous BCN suspension
was then mixed with styrene, emulsiļ¬ed using the same above-
described emulsifying protocol, and visualized (Figure 2b).
Despite this process being diļ¬€erent from the hexadecane one,
involving styrene, the BCNs displayed analogous interfacial pro-
perties for the styrene/water emulsion and a hexadecane/water
Figure 1. BCN morphology by TEM of a negatively stained dilute suspension of BCN.
7474 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
emulsion. The polymerization step served just as a ļ¬xing step
of the beads formed. We therefore assumed that the resulting
emulsion was representative of the present studied system.
Several very small noncovered white beads (diameter of the
beads was generally below 100 nm) were observed for all
the samples. These were artifactual outgrowths formed during
styrene polymerization. SEM images showed that the BCN
nanoparticles were evenly distributed at the surface and bent to
follow the curvation of each droplet. It means that the cellulosic
nanocrystals when wetted by the hydrophobic phase present
enough ļ¬‚exibility to bend along the surface. In other words, the
tension required for droplet formation is high enough to force
these colloidal particles to align without desorbing them. We can
assume that they will align preferentially according to the face
presenting the lower thickness which is 7 nm.
3.3. Emulsion Stability. Pickering emulsions were formulated
at a 30/70 ratio (o/w), with a 5 g/L suspension of BCN in
the water phase. These conditions were used to test stability
under various temperature conditions. Very high stability was
observed, without change in droplet size, even under various
mechanical treatments of the cream layer such as vortex or rotor
stator blender at 15 000 rpm. No variation in droplet size was
also observed after centrifugation or after keeping the samples
for 1 month at 4 Ā°C, at 40 Ā°C or up to 2 h at 80 Ā°C. These various
tests even after dilution were performed over months. The
absence of drop size variation in these conditions consolidates
the fact that irreversible adsorption occurs; indeed desorp-
tion might lead to phase separation, and this has never been
observed. Further tests were then carried out to specify stability
characteristics.
An emulsion is commonly considered stable if it is resistant to
physical changes over a practical length of time. It can be tested
by several methods including centrifugation, ļ¬ltration, shaking
or stirring, low intensity ultrasonic vibrations, or heating. All
the listed methods used for emulsion destabilization induce
mostly creaming or sedimentation, ļ¬‚occulation, and eventually
coalescence. Concretely, creaming forces contact (collision and
sticking) between the droplets and allows coalescence to occur
whereby the majority of the droplets merge creating fewer larger
droplets, thereby reducing the total interface area of the system.
As hexadecane has a lower density than water (d = 0.82 g/mL at
25 Ā°C), a creaming process was always observed. However
an emulsion can be considered stable as long as no coalescence
occurs; that is, the size and size distribution should not change.
When the emulsions were characterized over time, a stable drop
size was observed for several months although natural creaming
occurred. Centrifugation accelerates the creaming process,
forcing the droplets to concentrate. The excess water is then
excluded from the emulsion, leading to close packing conditions.
Centrifugation at 4000g was considered suitable for following the
resistance of droplets to coalescence. Two parameters were used
to characterize and evaluate the stability of the resulting emul-
sions: (i) the average drop size obtained after dispersion of a few
microliters of the cream in water and (ii) the volume of the
emulsion after centrifugation.
The ability of BCNs to stabilize the droplets was assessed by
varying the concentration of nanocrystals in the aqueous suspen-
sion from 0 to 5 g/L. Before centrifugation, the emulsion volume
increased regularly with the amount of BCN added, for a ļ¬xed oil
content (Figure 3). This indicated that trapping of the aqueous
phase was increased when a larger amount of BCNs was present.
After centrifugation at 4000g, the emulsion with concentrations
below 2 g/L of BCNs ā€œbroke upā€, and the emulsion volume could
no longer be measured. For concentrations above 2 g/L of BCNs,
dense white emulsions were obtained that resisted to the stress
induced by centrifugation.
The emulsion ratios, deļ¬ned as the volume of oil over the
volume of emulsion, were calculated and are shown in Figure 4.
At BCN concentrations below 2 g/L, the oil and water phases
separate and coalescence occurs by compression during the
centrifugation process. At higher BCN concentrations, the
percentage of oil trapped into the emulsion increases sharply
to reach a plateau value of around 0.7. This value is worth noting,
as it is close to the theoretical close packing condition of 0.74 for
monodispersed spheres. It is worth noting that the same limit
was observed whatever the centrifugation speed at 4000g and
10 000g, leading to the same packing conditions whatever the
BCN concentration. These droplets, that are resistant to cen-
trifugation, can also be dispersed in water and shaken without
disruption. The centrifugation deformed the droplets and ex-
cluded the water layers present at the interface without breaking
the droplets. The total volume of oil remained trapped within the
emulsion, with no modiļ¬cation of emulsion volume whatever the
concentration of BCN used, when centrifugation was stopped,
that is, after relaxation of the droplets. Above 2 g/L, the
emulsions displayed excellent mechanical resistance toward
deformation and coalescence.
3.4. Droplet Characterization. Droplet size variations were
monitored by measuring the surface mean diameter D(3,2) and
varying concentrations of BCN in the water phase for a fixed
amount of oil. Results are given for a ratio of 30/70 (o/w)
(Figure 5).
Droplet size showed a clear tendency to coalescence at the
lowest concentrations of BCN. Then sizes decreased to a plateau
Figure 2. Surface contribution of BCN. (a) Confocal laser scanning micrograph of droplets stabilized by BCN with double staining (hexadecane phase
stained with BODIPY564/570, BCN stained with calcoļ¬‚uor). (b and c) Scanning electron micrographs of styrene Pickering emulsion stabilized by BCN
and polymerized using V65 initiator.
7475 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
value of 4.2 Ī¼m diameter for all emulsions containing more than
2 g/L of BCNs in the water phase. The upper image in Figure 3
taken before centrifugation showed that the emulsion volume
increased regularly with the amount of BCNs. Below 2 g/L, the
increasing amount of BCN particles resulted in decreasing average
droplet size which led to a larger interfacial area and thus to a
higher emulsion volume. Similar coalescence tendency has been
previously reported for other types of Pickering emulsions.3,7,40
The method chosen to obtain our emulsions is based on a
limited coalescence41,40
process for the samples prepared with
the lowest BCN concentrations and up to 2 g/L. This occurs
when sonication produces a much larger area of the oil/water
interface than can potentially be covered by the nanocrystals.
When sonication is stopped, the partially unprotected droplets
coalesce. This coalescence results in a decrease of the oil/water
interface and stops as soon as the interface is suļ¬ƒciently covered.
For the samples prepared with the highest BCN concentrations,
at and above 2 g/L, a strong emulsion of stable droplet diameter
around 4 Ī¼m was obtained, irrespective of the amount of particles
added, which was resistant to deformation. The drop size limit
has rarely been discussed in literature. One argument comparing
the drop size according to the surface chemistry of the nano-
particles was analyzed in terms of emulsion stability. It was
observed that the droplets were smaller when more stable
emulsion conditions were used.9,42
In the present study, the
sonication process involved a rather high energy input with
production of submicrometer size droplets and the stability of
BCNs at the interface was signiļ¬cant. The size limitation might
therefore be due to the size and ļ¬‚exibility of the solid particles.
Indeed, BCNs consist of crystalline particles 855 nm in length,
and the size of the particles might be correlated to the droplet
size. No conclusions can be drawn from the present results,
but diļ¬€erent nanocrystal shapes can be produced according to
the cellulosic origin. The comparisons should be performed with
particles diļ¬€ering in morphology to validate this assumption.
3.5. Evaluation of Coverage. In order to check that the
particles had been irreversibly adsorbed at the o/w interface, the
particles remaining in the aqueous subphase after emulsification
and centrifugation were quantified by determining the sugar
content. No or negligible amounts of BCNs were found outside
the emulsion (data not shown) which meant that all the particles
introduced were involved in the emulsion, at the concentration
range under study.
A relationship between the mass of solid particles (mp) and the
average droplet diameter (D) has already been proposed.16
According to the equations proposed in section 2, the ļ¬nal
interfacial area should be controlled by mp. The average droplet
diameter (D) should then be inversely proportional to the
amount of solid particles included (mp):
1
D
Ā¼
mp
6hVdC
ư5ƞ
where C is the surface coverage, that is, the percentage of droplet
surface area covered by cellulosic particle, h is the thickness of the
BCN covering layer (7 nm for a monolayer), and Vd is the total
volume of the dispersed phase. The evolution of the inverse
diameter (1/D) for the various amounts of BCNs introduced
showed a linear increase, followed by stabilization at the higher
concentrations (Figure 6).
The ļ¬rst part of the plot increased linearly over the lower
concentrations, showing the same mode of coverage for all the
emulsions. This was observed up to a critical concentration
deļ¬ned by the deviation to linear mode in Figure 6. The tendency
to plateau shown by the second part of the curve would indicate
changes in the coverage arrangement.
These results indicate that when a limited amount of BCNs
is introduced, compared to the oil volume present, individual
droplets are produced for which the diameter is determined by
the amount of stabilizing particles available according to the
limited coalescence process. The coalescence process was
Figure 4. Ratio of hexadecane in the emulsions (v/v) measured after
centrifugation at 4000g for increasing BCN concentrations in the water
phase (g/L). The line serves to guide the eyes.
Figure 3. Hexadecane/aqueous BCN o/w emulsion stability (a) before centrifugation and (b) after centrifugation at 4000g for increasing BCN
concentration in the water phase from 0.1 to 5 g/L.
7476 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
observed up to a critical amount of 5.2 mg of BCNn added to
the water phase to stabilize 1 mL of hexadecane to produce the
droplet diameter of 4.2 Ī¼m. It corresponded to a concentration
of 2.2 g/L BCNn in the water phase as previously deļ¬ned.
Above this concentration, more and more nanocrystals can be
added without changing the droplet diameter. Cellulosic ma-
terials are known to aggregate in the aqueous phase via van der
Waals interactions and hydrogen bonding. The induced over-
load of material might result in ļ¬‚occulation due to particles
nonadsorbed or only partially adsorbed at the interface. This
would produce interconnected particles and change BCN
organization at the surface of the droplets resulting in the slope
variation.
Interface organization was investigated by calculating the
surface coverage according to eq 4, for emulsions prepared
with diļ¬€erent BCN concentrations. These values were then
plotted against mp, that is, the mass of BCN in the aqueous
phase, as shown in Figure 7, to characterize the packing density
of the BCN particles at the interface. At low concentrations,
the few droplets showed identical coverage up to 5.2 mg BCN/
mL hexadecane, the minimum required for stable droplets
having 60% coverage. After that, the percentage coverage
Figure 5. Droplet size dependence on BCN content (upper ļ¬gure) for droplet diameters D(3,2) vs BCN concentration in the water phase in an
emulsion containing hexadecane with a 30/70 oil/water ratio. (lower images) Transmission optical micrographs of the same emulsions; the
corresponding concentrations are given in the images.
Figure 6. Limited coalescence process visualized by the inverse D(3,2)
diameter plotted against the amount of particles included in the water
phase per milliliter of hexadecane.
Figure 7. Evolution of coverage vs the amount of particles included in
the water phase per milliliter of hexadecane for a 30/70 (o/w) ratio.
7477 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
increased to 100% for the highest BCN concentration tested,
that is, nearly 12 mg/mL hexadecane (which corresponds to a
suspension of 5 g/L BCN). This 60% coverage value is not
surprising, as values ranging from 22% to 70% have been
reported in the literature for other Pickering systems;40,43
even
a value as low as 8% was deļ¬ned for concentrated latex
micrometer-sized particles stabilized by nanosized spherical
silica particles.16
This coverage is deļ¬ned as the ratio of the area which could be
covered by the particles (length  width  amount of particles)
and the calculated total area of the oil droplets, taking into
account the D(3,2) drop diameter measured for each emulsion of
varying BCN concentration. The average BCN dimensions of
individual nanocrystals are used, measured by TEM and AFM
microscopies, without taking into account possible aggregation.
We can therefore assume that the measured available nanocrystal
surface and consequently the calculated coverage are overesti-
mates compared to the truly available area.
As the particles are irreversibly adsorbed at the interface and
the principle of Pickering stabilization results in partial wetting
adsorption, the formation of multilayers was unlikely. However,
above 5.2 mg/mL hexadecane, the percentage coverage increased
to even more than 100%. This could be attributed to the shape
of the particles, the elongated form and relative ļ¬‚exibility at the
surface leading to overlapping of the particles at high concentra-
tions. Thus, a simple geometric approach presents a limitation to
describe the BCN coverage properties due its intrinsic morpho-
logical and associative characteristics. This was checked by SEM
visualization of the droplet surface prepared by using BCN
concentrations of 0.5, 1, and 5 g/L. Figure 8 shows SEM images
of the polystyrene droplets covered by nanocrystals. Comparison
of the diļ¬€erent preparations revealed that, whatever the amount
of BCN introduced, the nanocrystals bent along the beads,
overlapping one over each other and eventually forming long
ļ¬bers. The tendency to aggregate inherent to the uncharged BCN
nanostructure was observed even at the lowest concentration.
However, coverage was lower for the emulsion prepared with the
0.5 g/L suspension, and greater overlapping of particles was
observed with the 5 g/L suspension.
Several papers highlighted the outstanding stabilizing proper-
ties of rodlike particles,26,44,45
and BCNs are generally assumed
to be rigid crystals with a high aspect ratio but their thickness of
7 nm allows a certain ļ¬‚exibility when aligned along the droplet
interface. We therefore never observed any ā€œnestlikeā€ structures
as obtained for very rigid particles such as CaCO3.46
Finally, if
this ļ¬‚exibility is the limitation point, the plateau observed for
droplet size around 4 Ī¼m in diameter might be correlated with
this ability of the BCNs to bend. As a result, it would also be the
main explanation to the break point observed in Figure 6. Once
the maximum curvature of the particles is reached, the interface
area is ļ¬xed and adding BCNs induces a new coverage organiza-
tion. However, if the strength necessary to stay bent at the
interface becomes high, the particles might then desorb from the
interface while we observed a very high stability of these drops.
The BCNs present the particularity to self-associate, and what-
ever the concentration a more or less densely packed 2D network
forms at the surface of the droplets. This network is highly stable
both because the energy of adsorption prevents the particles
from being removed from the interface and because particle
aggregation prevents coalescence. Steric hindrance appears to be
the major mechanism responsible for droplet stability.47
The
strongadhesionofparticlestothe interfaceconfers to the emulsion
high resistance to coalescence and high stability. This has to be
attributed to the particular behavior of cellulosic derivatives, that is,
their elongated shape and the low charged surface chemistry
forming an entangled network of isolated nanocrystals.
ConsideringBCNs themselves, these quasi-neutral particles are
generally considered as hydrophilic matter, but they can stabilize
at the oil/water interface. Being regular crystalline particles, they
are organized according to various crystalline plans and some
of these plans expose a more hydrophobic surface.48
When well
oriented, this may promote the particle interfacial properties. As a
result, the BCNs prepared present both hydrophilic and hydro-
phobic characters in a good ratio. Indeed, with higher surface
charged density, they do not stabilize emulsions because their too
high aļ¬ƒnity for the aqueous phase prevents stabilization at the
o/w interface. On the other hand, the absence of charge would
induce formation of big aggregates unable to form individual
Figure 8. SEM images for metallization of a polymerized styrene/water emulsion stabilized by BCN suspensions, from left to right, at 0.5, 1, and 5 g/L.
7478 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
droplets. Contact angle determination is diļ¬ƒcult to conduct at
the liquid ļ¬‚uid interface; however, some methods such as the one
developed by Paunov49
might help to understand the attachment
of the particles to the interface. As a result, bearing no chemical
function and resisting to high acid hydrolysis, the present BCNs
allow droplet stabilization over a large domain of pH, time, and
temperature.
Bacterial cellulose nanocrystals present, for example, an
aspect ratio signiļ¬cantly larger than that of wood and cotton
nanocrystals.34
For further emulsion studies, it is known that cel-
lulosic nanoparticles varying in shape (length and aspect ratios)
can be produced according to the cellulose origin (cotton, algae,
animal) or after treatments such as recrystallization (regenerated
cellulose II). From the literature, various lengths can be obtained
from some tens of nanometers to several micrometers. Since the
coverage organization can be modiļ¬ed by the crystal morphol-
ogy, we can expect variations in the emulsion characteristics
particularly from the curvature adaptability and networking
aptitude. Their shape versatility and high stability added to their
biorenewable property as raw material make the present BCNs or
other cellulosic derivatives outstanding sources for study of the
Pickering interfacial stabilization process and large application
domains such as for cosmetic, medical, or food industry notably.
4. CONCLUSIONS
Bacterial cellulosic nanocrystals were produced by hydrochlo-
ric acid hydrolysis and resulted in nanoparticles of very low
charge density. After sonication, they resulted in a suspension
stable for several months. This process provided nanosized
cellulosic particles which were directly able to stabilize irrever-
sibly an oil in water Pickering emulsion. BCNs can therefore be
used to prepare a monodispersed emulsion without any further
modiļ¬cation or wrapping process.
The emulsions produced have been characterized and proved
to be stable over months whatever the BCN concentration as
long as no centrifugation was performed. However, above a limit
evaluated at 5.2 mg of BCN to stabilize 1 mL of hexadecane, an
emulsion able to be dispersed in water and resistant to centrifu-
gation at 4000g was obtained.
Studies varying the amounts of nanoparticles were carried out
to investigate the surface organization of the droplets stabilized by
BCNs. At the lowest concentrations, limited coalescence occurred
and the droplet size decreased up to about 4 Ī¼m diameter.
Droplets with a constant surface coverage of 60% were formed,
which represents for our system the minimum required tostabilize
the emulsion. When more than 5.2 mg of BCN/mL of hexadecane
was introduced, the BCN particles were in excess and presented a
much greater available surface area than was required to stabilize
4 Ī¼m diameter droplets. The surface coverage increased toward
100% as the amounts of added BCN were increased. However, no
BCN was found in the aqueous phase after centrifugation. We
propose that irreversible adsorption of the particles, associated
with steric hindrance of the 2D network formed, at the interface
was responsible for the very high droplet stability obtained.
ā€™ ASSOCIATED CONTENT
b
S Supporting Information. Additionnal results about the
BCN surface charge density by conductometric titration and
thickness by AFM determination. This material is available free
of charge via the Internet at http://pubs.acs.org.
ā€™ AUTHOR INFORMATION
Corresponding Author
*E-mail: capron@nantes.inra.fr. Telephone: 33(0)240675095.
ā€™ ACKNOWLEDGMENT
The authors thank Brigitte Bouchet for assistance in TEM
experiments (BIBS platform, INRA Nantes, France), Nicolas
Stephan for assistance in SEM experiments (IMN, Nantes,
France), Patricia Bertoncini for AFM measurements, Solene
Grosbois for excellent technical assistance, and R
egion Pays de
la Loire (RMB network) for ļ¬nancial support.
ā€™ REFERENCES
(1) Ramsden, W. Proc. R. Soc. 1903, 72, 156.
(2) Pickering, S. U. J. Chem. Soc. 1907, 91, 2001.
(3) Tambe, E. T.; Sharma, M. M. J. Colloid Interface Sci. 1993,
157, 244ā€“253.
(4) Binks, B. P.; Lumsdon, S. O. Langmuir 2001, 17, 4540ā€“4547.
(5) Pieranski, P. Phys. Rev. Lett. 1980, 45, 569ā€“572.
(6) Binks, B. P. Curr. Opin. Colloid Interface Sci. 2002, 7, 21ā€“41.
(7) Aveyard, R.; Binks, B. P.; Clint, J. H. Adv. Colloid Interface Sci.
2003, 100, 503ā€“546.
(8) Finkle, P.; Draper, H. D.; H., H. J. J. Am. Chem. Soc. 1923,
45, 2780ā€“2788.
(9) Binks, B. P.; Lumsdon, S. O. Langmuir 2000, 16, 8622ā€“8631.
(10) Binks, B. P.; Philip, J.; Rodrigues, J. A. Langmuir 2005, 21,
3296ā€“3302.
(11) Midmore, B. R. Colloids Surf., A 1998, 132, 257ā€“265.
(12) Colard, C. A. L.; Teixeira, R. F. A.; Bon, S. A. F. Langmuir 2010,
26, 7915ā€“7921.
(13) Tsugita, A.; Takemoto, S.; Mori, K.; Yoneya, T.; Otani, Y.
J. Colloid Interface Sci. 1983, 95, 551ā€“560.
(14) Bon, S. A. F.; Colver, P. J. Langmuir 2007, 23, 8316ā€“8322.
(15) Cui, Z. G.; Shi, K. Z.; Cui, Y. Z.; Binks, B. P. Colloids Surf., A
2008, 329, 67ā€“74.
(16) Gautier, F.; Destribats, M.; Perrier-Cornet, R.; Dechezelles,
J. F.; Giermanska, J.; Heroguez, V.; Ravaine, S.; Leal-Calderon, F.;
Schmitt, V. Phys. Chem. Chem. Phys. 2007, 9, 6455ā€“6462.
(17) Grosse, I.; Estel, K. Colloid Polym. Sci. 2000, 278, 1000ā€“1006.
(18) Binks, B. P.; Rodrigues, J. A.; Frith, W. J. Langmuir 2007, 23,
3626ā€“3636.
(19) Ougiya, H.; Watanabe, K.; Morinaga, Y.; Yoshinaga, F. Biosci.,
Biotechnol., Biochem. 1997, 61, 1541ā€“1545.
(20) Blaker, J. J.; Lee, K. Y.; Li, X. X.; Menner, A.; Bismarck, A. Green
Chem. 2009, 11, 1321ā€“1326.
(21) Yusoļ¬€, A.; Murray, B. S. Food Hydrocolloids 2011, 25, 42ā€“55.
(22) French, A. D.; Bertoniere, N. R.; Brown, R. M.; Chanzy, H.;
Gray, D. G.; Hattori, K.; Glasser, W. G. In Encyclopedia of Polymer Science
and Technology, 3rd ed.; Kroschwitz, J. I., Ed.; John Wiley  Sons:
New York, 2003; pp 473507.
(23) Rowland, S. P.; Roberts, E. J. J. Polym. Sci., Part A: Polym. Chem.
1972, 10, 867ā€“879.
(24) Eichhorn, S. J.; Dufresne, A.; Aranguren, M.; Marcovich, N. E.;
Capadona, J. R.; Rowan, S. J.; Weder, C.; Thielemans, W.; Roman, M.;
Renneckar, S.; Gindl, W.; Veigel, S.; Keckes, J.; Yano, H.; Abe, K.; Nogi,
M.; Nakagaito, A. N.; Mangalam, A.; Simonsen, J.; Benight, A. S.;
Bismarck, A.; Berglund, L. A.; Peijs, T. J. Mater. Sci. 2010, 45, 1ā€“33.
(25) Oza, K. P.; Frank, S. G. J. Dispersion Sci. Technol. 1986, 7,
543ā€“561.
(26) Wege, H. A.; Kim, S.; Paunov, V. N.; Zhong, Q. X.; Velev, O. D.
Langmuir 2008, 24, 9245ā€“9253.
(27) Jonoobi, M.; Harun, J.; Mathew, A. P.; Hussein, M. Z. B.;
Oksman, K. Cellulose 2010, 17, 299ā€“307.
7479 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479
Langmuir ARTICLE
(28) Andresen, M.; Stenius, P. J. Dispersion Sci. Technol. 2007, 28,
837ā€“844.
(29) Wagberg, L.; Decher, G.; Norgren, M.; Lindstrom, T.; Ankerfors,
M.; Axnas, K. Langmuir 2008, 24, 784ā€“795.
(30) Ranby, B. G. Discuss. Faraday Soc. 1951, 11, 158ā€“164.
(31) Elazzouzi-Hafraoui, S.; Nishiyama, Y.; Putaux, J. L.; Heux, L.;
Dubreuil, F.; Rochas, C. Biomacromolecules 2008, 9, 57ā€“65.
(32) Samir, M.; Alloin, F.; Dufresne, A. Biomacromolecules 2005,
6, 612ā€“626.
(33) Gilkes, N. R.; Jervis, E.; Henrissat, B.; Tekant, B.; Miller, R. C.;
Warren, R. A. J.; Kilburn, D. G. J. Biol. Chem. 1992, 267, 6743ā€“6749.
(34) Araki, J.; Kuga, S. Langmuir 2001, 17, 4493ā€“4496.
(35) Araki, J.; Wada, M.; Kuga, S.; Okano, T. Colloids Surf., A 1998,
142, 75ā€“82.
(36) Hirai, A.; Inui, O.; Horii, F.; Tsuji, M. Langmuir 2009, 25,
497ā€“502.
(37) Grunert, M.; Winter, W. T. J. Polym. Environ. 2002, 10, 27ā€“30.
(38) Habibi, Y.; Lucia, L. A.; Rojas, O. J. Chem. Rev. 2010, 110,
3479ā€“3500.
(39) Haase, M. F.; Grigoriev, D.; Moehwald, H.; Tiersch, B.;
Shchukin, D. G. Langmuir 2011, 27, 74ā€“82.
(40) Arditty, S.; Whitby, C. P.; Binks, B. P.; Schmitt, V.; Leal-Calderon,
F. Eur. Phys. J. E 2003, 12, 355ā€“355.
(41) Whitesides, T. H.; Ross, D. S. J. Colloid Interface Sci. 1995,
169, 48ā€“59.
(42) Frelichowska, J.; Bolzinger, M. A.; Chevalier, Y. J. Colloid
Interface Sci. 2010, 351, 348ā€“356.
(43) Nie, Z. H.; Il Park, J.; Li, W.; Bon, S. A. F.; Kumacheva, E. J. Am.
Chem. Soc. 2008, 130, 16508ā€“16509.
(44) Madivala, B.; Vandebril, S.; Fransaer, J.; Vermant, J. Soft Matter
2009, 5, 1717ā€“1727.
(45) Alargova, R. G.; Warhadpande, D. S.; Paunov, V. N.; Velev,
O. D. Langmuir 2004, 20, 10371ā€“10374.
(46) Zhou, W. Z.; Cao, J.; Liu, W. C.; Stoyanov, S. Angew. Chem., Int.
Ed. 2009, 48, 378ā€“381.
(47) Lopetinsky, R.; Masliyah, J.; Zhenghe, X. Solid stabilized
emulsion: A review. In Colloidal particles at liquid interfaces; Binks,
B. P., Horozov, T. S., Eds.; Cambridge University Press: Cambridge,
2006; Vol. Chap. 6, pp 185224.
(48) Mazeau, K.; Rivet, A. Biomacromolecules 2008, 9, 1352ā€“1354.
(49) Paunov, V. N. Langmuir 2003, 19, 7970ā€“7976.
View publication stats
View publication stats

More Related Content

What's hot

What's hot (19)

Coagulation and FLOCCULATION
Coagulation and FLOCCULATIONCoagulation and FLOCCULATION
Coagulation and FLOCCULATION
Ā 
calcium hydroxide
calcium hydroxidecalcium hydroxide
calcium hydroxide
Ā 
Coagulants
CoagulantsCoagulants
Coagulants
Ā 
Calcium hydroxide cements
Calcium hydroxide cementsCalcium hydroxide cements
Calcium hydroxide cements
Ā 
CALCIUM HYDROXIDE IN CONSERVATIVE DENTISTRY
CALCIUM HYDROXIDE IN CONSERVATIVE DENTISTRYCALCIUM HYDROXIDE IN CONSERVATIVE DENTISTRY
CALCIUM HYDROXIDE IN CONSERVATIVE DENTISTRY
Ā 
Firas abu jaber
Firas abu jaberFiras abu jaber
Firas abu jaber
Ā 
Cellulose
CelluloseCellulose
Cellulose
Ā 
IRJET- Experimental Investigation on Development of Self Healing Mortar u...
IRJET-  	  Experimental Investigation on Development of Self Healing Mortar u...IRJET-  	  Experimental Investigation on Development of Self Healing Mortar u...
IRJET- Experimental Investigation on Development of Self Healing Mortar u...
Ā 
Effect of UV Treatment on the Degradation of Biodegradable Polylactic Acid
Effect of UV Treatment on the Degradation of Biodegradable Polylactic AcidEffect of UV Treatment on the Degradation of Biodegradable Polylactic Acid
Effect of UV Treatment on the Degradation of Biodegradable Polylactic Acid
Ā 
Water treatment-lecture-3-eenv
Water treatment-lecture-3-eenvWater treatment-lecture-3-eenv
Water treatment-lecture-3-eenv
Ā 
F05722530
F05722530F05722530
F05722530
Ā 
CALCIUM HYDROXIDE IN ENDODONTICS
CALCIUM HYDROXIDE IN ENDODONTICSCALCIUM HYDROXIDE IN ENDODONTICS
CALCIUM HYDROXIDE IN ENDODONTICS
Ā 
Plant chemistry RO system
Plant chemistry RO system Plant chemistry RO system
Plant chemistry RO system
Ā 
Reverse Osmosis Based Desalination
Reverse Osmosis Based DesalinationReverse Osmosis Based Desalination
Reverse Osmosis Based Desalination
Ā 
Efecto de hierro antiescalas
Efecto de hierro antiescalasEfecto de hierro antiescalas
Efecto de hierro antiescalas
Ā 
International Concrete Sustainability Conference 2013 Bijoy
International Concrete Sustainability Conference 2013 Bijoy International Concrete Sustainability Conference 2013 Bijoy
International Concrete Sustainability Conference 2013 Bijoy
Ā 
Coagulation and sedimentation
Coagulation and sedimentationCoagulation and sedimentation
Coagulation and sedimentation
Ā 
Cellulose Based Materials: in-Depth Property Survey And Assessment
Cellulose Based Materials: in-Depth Property Survey And AssessmentCellulose Based Materials: in-Depth Property Survey And Assessment
Cellulose Based Materials: in-Depth Property Survey And Assessment
Ā 
Self-healing concrete
Self-healing concreteSelf-healing concrete
Self-healing concrete
Ā 

Similar to evaluation of stability of formulations.pdf

Cubosome - A Review
Cubosome - A ReviewCubosome - A Review
Cubosome - A Review
ijtsrd
Ā 
Aquasomes, principle,methods,
Aquasomes, principle,methods,Aquasomes, principle,methods,
Aquasomes, principle,methods,
HARISH C
Ā 
Hashaikeh 2007 Fuel
Hashaikeh 2007 FuelHashaikeh 2007 Fuel
Hashaikeh 2007 Fuel
Jalal Hawari
Ā 

Similar to evaluation of stability of formulations.pdf (20)

Chanukya & Rastogi, JCTBT, 09
Chanukya & Rastogi, JCTBT, 09Chanukya & Rastogi, JCTBT, 09
Chanukya & Rastogi, JCTBT, 09
Ā 
Niosomes
NiosomesNiosomes
Niosomes
Ā 
NANOCELLULOSE PPT.pptx
NANOCELLULOSE PPT.pptxNANOCELLULOSE PPT.pptx
NANOCELLULOSE PPT.pptx
Ā 
Essay On Down Membrane
Essay On Down MembraneEssay On Down Membrane
Essay On Down Membrane
Ā 
Aquasomes
AquasomesAquasomes
Aquasomes
Ā 
Cubosome - A Review
Cubosome - A ReviewCubosome - A Review
Cubosome - A Review
Ā 
10.1016@j.carbpol.2011.04.046.pdf
10.1016@j.carbpol.2011.04.046.pdf10.1016@j.carbpol.2011.04.046.pdf
10.1016@j.carbpol.2011.04.046.pdf
Ā 
Aquasomes KKR
Aquasomes KKRAquasomes KKR
Aquasomes KKR
Ā 
Manufacturing of important polymers and polymer processing
Manufacturing of important polymers and polymer processing Manufacturing of important polymers and polymer processing
Manufacturing of important polymers and polymer processing
Ā 
Training process manual for wtp narmada
Training  process manual for wtp narmadaTraining  process manual for wtp narmada
Training process manual for wtp narmada
Ā 
AQUASOMES: A NOVEL CARRIER FOR DRUG DELIVERY SYSTEM
AQUASOMES: A NOVEL CARRIER FOR DRUG DELIVERY SYSTEMAQUASOMES: A NOVEL CARRIER FOR DRUG DELIVERY SYSTEM
AQUASOMES: A NOVEL CARRIER FOR DRUG DELIVERY SYSTEM
Ā 
Phytosome
PhytosomePhytosome
Phytosome
Ā 
Aquasomes, principle,methods,
Aquasomes, principle,methods,Aquasomes, principle,methods,
Aquasomes, principle,methods,
Ā 
New emerging water treatment methods
New emerging water treatment methodsNew emerging water treatment methods
New emerging water treatment methods
Ā 
Cubosomes
CubosomesCubosomes
Cubosomes
Ā 
Romsta
RomstaRomsta
Romsta
Ā 
Hashaikeh 2007 Fuel
Hashaikeh 2007 FuelHashaikeh 2007 Fuel
Hashaikeh 2007 Fuel
Ā 
Recent advances in formulation aspects & manufacturing of semisolids
Recent advances in formulation aspects & manufacturing of semisolidsRecent advances in formulation aspects & manufacturing of semisolids
Recent advances in formulation aspects & manufacturing of semisolids
Ā 
2018 - Flexible and porous cellulose aerogels-zeolitic imidazolate framework ...
2018 - Flexible and porous cellulose aerogels-zeolitic imidazolate framework ...2018 - Flexible and porous cellulose aerogels-zeolitic imidazolate framework ...
2018 - Flexible and porous cellulose aerogels-zeolitic imidazolate framework ...
Ā 
H1802034450
H1802034450H1802034450
H1802034450
Ā 

More from RupajitBhattacharjee1 (11)

industrial microbial culture (1).pdf
industrial microbial culture (1).pdfindustrial microbial culture (1).pdf
industrial microbial culture (1).pdf
Ā 
pharmacology_mcq.pdf
pharmacology_mcq.pdfpharmacology_mcq.pdf
pharmacology_mcq.pdf
Ā 
positive control.pdf
positive control.pdfpositive control.pdf
positive control.pdf
Ā 
gas sterilization.pdf
gas sterilization.pdfgas sterilization.pdf
gas sterilization.pdf
Ā 
Phytochemicalevaluation.pdf
Phytochemicalevaluation.pdfPhytochemicalevaluation.pdf
Phytochemicalevaluation.pdf
Ā 
bacteriostatic test.pdf
bacteriostatic test.pdfbacteriostatic test.pdf
bacteriostatic test.pdf
Ā 
Nanosuspension
Nanosuspension Nanosuspension
Nanosuspension
Ā 
phenolic disinfactants moa.pdf
phenolic disinfactants moa.pdfphenolic disinfactants moa.pdf
phenolic disinfactants moa.pdf
Ā 
Anaerobic_bacteria_culture__Practical_-1.pdf
Anaerobic_bacteria_culture__Practical_-1.pdfAnaerobic_bacteria_culture__Practical_-1.pdf
Anaerobic_bacteria_culture__Practical_-1.pdf
Ā 
disinfactant.pdf
disinfactant.pdfdisinfactant.pdf
disinfactant.pdf
Ā 
Rupajit Bhattacharjee hypertension management
Rupajit Bhattacharjee hypertension management Rupajit Bhattacharjee hypertension management
Rupajit Bhattacharjee hypertension management
Ā 

Recently uploaded

Recently uploaded (20)

Tį»”NG ƔN Tįŗ¬P THI VƀO Lį»šP 10 MƔN TIįŗ¾NG ANH NĂM Hį»ŒC 2023 - 2024 CƓ ĐƁP ƁN (NGį»® Ƃ...
Tį»”NG ƔN Tįŗ¬P THI VƀO Lį»šP 10 MƔN TIįŗ¾NG ANH NĂM Hį»ŒC 2023 - 2024 CƓ ĐƁP ƁN (NGį»® Ƃ...Tį»”NG ƔN Tįŗ¬P THI VƀO Lį»šP 10 MƔN TIįŗ¾NG ANH NĂM Hį»ŒC 2023 - 2024 CƓ ĐƁP ƁN (NGį»® Ƃ...
Tį»”NG ƔN Tįŗ¬P THI VƀO Lį»šP 10 MƔN TIįŗ¾NG ANH NĂM Hį»ŒC 2023 - 2024 CƓ ĐƁP ƁN (NGį»® Ƃ...
Ā 
HMCS Max Bernays Pre-Deployment Brief (May 2024).pptx
HMCS Max Bernays Pre-Deployment Brief (May 2024).pptxHMCS Max Bernays Pre-Deployment Brief (May 2024).pptx
HMCS Max Bernays Pre-Deployment Brief (May 2024).pptx
Ā 
Application orientated numerical on hev.ppt
Application orientated numerical on hev.pptApplication orientated numerical on hev.ppt
Application orientated numerical on hev.ppt
Ā 
This PowerPoint helps students to consider the concept of infinity.
This PowerPoint helps students to consider the concept of infinity.This PowerPoint helps students to consider the concept of infinity.
This PowerPoint helps students to consider the concept of infinity.
Ā 
Single or Multiple melodic lines structure
Single or Multiple melodic lines structureSingle or Multiple melodic lines structure
Single or Multiple melodic lines structure
Ā 
Spatium Project Simulation student brief
Spatium Project Simulation student briefSpatium Project Simulation student brief
Spatium Project Simulation student brief
Ā 
Sensory_Experience_and_Emotional_Resonance_in_Gabriel_Okaras_The_Piano_and_Th...
Sensory_Experience_and_Emotional_Resonance_in_Gabriel_Okaras_The_Piano_and_Th...Sensory_Experience_and_Emotional_Resonance_in_Gabriel_Okaras_The_Piano_and_Th...
Sensory_Experience_and_Emotional_Resonance_in_Gabriel_Okaras_The_Piano_and_Th...
Ā 
HMCS Vancouver Pre-Deployment Brief - May 2024 (Web Version).pptx
HMCS Vancouver Pre-Deployment Brief - May 2024 (Web Version).pptxHMCS Vancouver Pre-Deployment Brief - May 2024 (Web Version).pptx
HMCS Vancouver Pre-Deployment Brief - May 2024 (Web Version).pptx
Ā 
How to Give a Domain for a Field in Odoo 17
How to Give a Domain for a Field in Odoo 17How to Give a Domain for a Field in Odoo 17
How to Give a Domain for a Field in Odoo 17
Ā 
Mehran University Newsletter Vol-X, Issue-I, 2024
Mehran University Newsletter Vol-X, Issue-I, 2024Mehran University Newsletter Vol-X, Issue-I, 2024
Mehran University Newsletter Vol-X, Issue-I, 2024
Ā 
On National Teacher Day, meet the 2024-25 Kenan Fellows
On National Teacher Day, meet the 2024-25 Kenan FellowsOn National Teacher Day, meet the 2024-25 Kenan Fellows
On National Teacher Day, meet the 2024-25 Kenan Fellows
Ā 
SOC 101 Demonstration of Learning Presentation
SOC 101 Demonstration of Learning PresentationSOC 101 Demonstration of Learning Presentation
SOC 101 Demonstration of Learning Presentation
Ā 
General Principles of Intellectual Property: Concepts of Intellectual Proper...
General Principles of Intellectual Property: Concepts of Intellectual  Proper...General Principles of Intellectual Property: Concepts of Intellectual  Proper...
General Principles of Intellectual Property: Concepts of Intellectual Proper...
Ā 
Towards a code of practice for AI in AT.pptx
Towards a code of practice for AI in AT.pptxTowards a code of practice for AI in AT.pptx
Towards a code of practice for AI in AT.pptx
Ā 
ICT Role in 21st Century Education & its Challenges.pptx
ICT Role in 21st Century Education & its Challenges.pptxICT Role in 21st Century Education & its Challenges.pptx
ICT Role in 21st Century Education & its Challenges.pptx
Ā 
Micro-Scholarship, What it is, How can it help me.pdf
Micro-Scholarship, What it is, How can it help me.pdfMicro-Scholarship, What it is, How can it help me.pdf
Micro-Scholarship, What it is, How can it help me.pdf
Ā 
Kodo Millet PPT made by Ghanshyam bairwa college of Agriculture kumher bhara...
Kodo Millet  PPT made by Ghanshyam bairwa college of Agriculture kumher bhara...Kodo Millet  PPT made by Ghanshyam bairwa college of Agriculture kumher bhara...
Kodo Millet PPT made by Ghanshyam bairwa college of Agriculture kumher bhara...
Ā 
Understanding Accommodations and Modifications
Understanding  Accommodations and ModificationsUnderstanding  Accommodations and Modifications
Understanding Accommodations and Modifications
Ā 
SKILL OF INTRODUCING THE LESSON MICRO SKILLS.pptx
SKILL OF INTRODUCING THE LESSON MICRO SKILLS.pptxSKILL OF INTRODUCING THE LESSON MICRO SKILLS.pptx
SKILL OF INTRODUCING THE LESSON MICRO SKILLS.pptx
Ā 
Sociology 101 Demonstration of Learning Exhibit
Sociology 101 Demonstration of Learning ExhibitSociology 101 Demonstration of Learning Exhibit
Sociology 101 Demonstration of Learning Exhibit
Ā 

evaluation of stability of formulations.pdf

  • 1. See discussions, stats, and author profiles for this publication at: https://www.researchgate.net/publication/51158161 New Pickering Emulsions Stabilized by Bacterial Cellulose Nanocrystals ArticleĀ Ā inĀ Ā Langmuir Ā· June 2011 DOI: 10.1021/la200971fĀ Ā·Ā Source: PubMed CITATIONS 529 READS 2,128 4 authors, including: Some of the authors of this publication are also working on these related projects: innovation management and sustainability - Safer-by-Design View project Modelling and assessment of a small scale flexible biorefinery in urban and peri-urban areas in Nantes and Hamburg. View project Irina Kalashnikova 23 PUBLICATIONSĀ Ā Ā 1,670 CITATIONSĀ Ā Ā  SEE PROFILE Bernard Cathala French National Institute for Agriculture, Food, and Environment (INRAE) 146 PUBLICATIONSĀ Ā Ā 5,426 CITATIONSĀ Ā Ā  SEE PROFILE Isabelle Capron French National Institute for Agriculture, Food, and Environment (INRAE) 74 PUBLICATIONSĀ Ā Ā 4,023 CITATIONSĀ Ā Ā  SEE PROFILE All content following this page was uploaded by Irina Kalashnikova on 20 December 2017. The user has requested enhancement of the downloaded file.
  • 2. Published: May 23, 2011 r 2011 American Chemical Society 7471 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 ARTICLE pubs.acs.org/Langmuir New Pickering Emulsions Stabilized by Bacterial Cellulose Nanocrystals Irina Kalashnikova, Herv e Bizot, Bernard Cathala, and Isabelle Capron* UR 1268 Biopolym eres, Interactions et Assemblages, INRA, F-44316 Nantes, France b S Supporting Information 1. INTRODUCTION An emulsion is a system of dispersed droplets of one im- miscible liquid in another stabilized by emulsiļ¬ers. Since the pioneering work of Ramsden1 and Pickering,2 solid colloidal particles have been shown to adsorb at ļ¬‚uid interfaces to form so-called ā€œPickering emulsionsā€. The properties of these systems are due in part to the irreversible nature of such particle adsorption.35 Interest in Pickering emulsions has been renewed over the past 10 years, especially for health and cosmetics applications where the use of surfactants is undesirable. Indeed, they not only present good mechanical properties, but much fewer particles are required to produce good stability, thereby leading to a reduction in the use of hazardous surfactants and their environmental consequences.6,7 Stabilization of solid particles at the interface is generally considered to be directed by particle wettability, which is itself directed by the more or less hydrophilic/hydrophobic nature of the surface. The formation of an oil in water (o/w) emulsion will occur for hydrophilic surfaces. On the opposite, a stable water-in- oil (w/o) emulsion will be produced for hydrophobic surfaces.8 If the particles are completely wetted by water or oil, they may remain dispersed in either phase and no stable emulsion will form.9 Most of the literature dealing with Pickering stabilization concerns various types of inorganic, commercially available particles such as silica,4,1012 montmorillonite,13 Laponite,14 calcium carbonate,3,15 carbon graphite,3 or various latexes.4,16 However the raw, non-surface-treated nanoparticles are usually not surface active due to their lack of hydrophilicity/hydropho- bicity, or great tendency to aggregate. Methods involving surface modiļ¬cations6 or the addition of cosurfacting compounds17,18 have been developed to produce symmetrical or asymmetrical (Janus) particles, but such methods increase the use of chemicals and make the process complicated for large-scale production. Research eļ¬€orts are being focused on the development of environmentally friendly, biobased nanocomposites, but few studies, up to now, have described stabilization by particles derived from renewable resources.1921 Cellulose is one of the most widespread biopolymers and is a good candidate because of its sustainability, biodegradability, and nontoxicity. Cellulose is a linear homopolymer of Ī²(1-4)-D-glucose resi- dues linked together by glycosidic oxygen bridges. It exists in nature as highly resistant ļ¬bers. The high cohesive energy is induced by van der Waals forces and by extensive hydrogen bond networks within and between the chains via the hydroxyl groups in equatorial position.22 These ļ¬bers are formed by the stacking of microļ¬brils, and it is now recognized that the ordered crystal- line regions are interrupted by amorphous or less ordered regions along the elementary ļ¬bril where the microļ¬brils are distorted by internal strain.23,24 A few investigations have used cellulose derivatives such as microļ¬brillated cellulose (MFC), which are moderately de- graded microļ¬brils (510 Ī¼m long), to stabilize oil in water emulsions,19,25 but their long length compared to the size of the droplets produced networks rather than individual drops. In order to control the emulsion characteristics, the particle size must be reduced. Concerning interfacial stabilization, most of the studies have been carried out on hydrophobically modiļ¬ed cellulosic material26 leading to water in oil emulsions. They Received: March 15, 2011 Revised: May 9, 2011 ABSTRACT: We studied oil in water Pickering emulsions stabilized by cellulose nanocrystals obtained by hydrochloric acid hydrolysis of bacterial cellulose. The resulting solid particles, called bacterial cellu- lose nanocrystals (BCNs), present an elongated shape and low surface charge density, forming a colloidal suspension in water. The BCNs produced proved to stabilize the hexadecane/water interface, promot- ing monodispersed oil in water droplets around 4 Ī¼m in diameter stable for several months. We characterized the emulsion and visua- lized the particles at the surface of the droplets by scanning electron microscopy (SEM) and calculated the droplet coverage by varying the BCN concentration in the aqueous phase. A 60% coverage limit has been deļ¬ned, above which very stable, deformable droplets are obtained. The high stability of the more covered droplets was attributed to the particle irreversible adsorption associated with the formation of a 2D network. Due to the sustainability and low environmental impact of cellulose, the BCN based emulsions open opportunities for the development of environmentally friendly new materials.
  • 3. 7472 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE involved acetylated nanoļ¬bers,27,20 sililated microļ¬brils,28 or carboxymethylated cellulose,29 but none reported the production of stable oil in water droplets. It has been known for many years that stable nanoparticle suspensions can be prepared by treating native cellulose to harsh acid hydrolysis.30,31 Acid hydrolysis is a heterogeneous process which involves ļ¬rst the diļ¬€usion of acid into the ļ¬bers followed by the cleavage of the glycosidic bonds, resulting in a turbid colloidal suspension. Sulfuric acid is commonly used in introdu- cing sulfated charges at the surface. The absence of charge generally leads to the production of crystalline aggregates.32 In the literature, these crystallites are referred to as whiskers or nanocrystalline cellulose. In this work, cellulose nanoparticles were prepared via hydro- chloric acid hydrolysis of bacterial cellulose. The bacterial cellulose was chosen on its availability since it can be easily produced from nata de coco, in which cellulose is present at rather high concentration. Moreover, it is possible to get it wet, whereas most of the other sources available provide dry material and present limited contaminants, that is, without any hemi- cellulose or various byproduct generally surrounding cellulose. It is then possible to hydrolyze it with milder conditions and, notably, to avoid the use of sulfuric acid which promotes highly charged surfaces. Finally, characteristic features of bacterial cellulose nanocrystals (BCNs) are their large aspect ratios and ļ¬‚at, ribbonlike cross sections. As a result, pure low charged BCNs were used, without further desulfation, modiļ¬cation, or addition of any cosurfacting product, to stabilize the interface of an oil in water emulsion. These BCNs were characterized, and the stability of the emulsion, drop size, and coverage characteristics were investigated. 2. MATERIALS AND METHODS 2.1. Materials. Nata de coco was a gift from Mrs. Joann Dar, who bought it in San Jose (Central Luzon, Philippines) from a traditional producer. All other products were purchased at 99% or greater purity. n-Hexadecane (Sigma) was cleaned thoroughly with water to remove any remaining surfactants. Styrene (Fluka) was purified: tert-butylcate- chol inhibitor was removed by percolation through a cartridge filled with activated alumina (EcoChrom N super1) regenerated by treatment at 400 Ā°C. Polymerization was initiated with V65 (2,20 -azobis(2,4-dimethyl valeronitrile)) which was a gift from Qingdao Runxing Photoelectric Material Co. (LTD, Qingdao, China). For CLSM BODIPY (4,4- difluoro-4-bora-3a,4a-diaza-s-indacene) (Molecular Probes Invitrogen, Eugene, OR) and calcofluor (Sigma) were used without purification. 2.2. BCN Preparation. BCNs were obtained from nata de coco cubes ground in a Waring blender at maximum speed. The resulting slurry was filtered and resuspended in 0.5 N NaOH and then stirred in a lidded flask for 2 h at 70 Ā°C. Alkali was removed by rinsing with distilled water to neutrality. After that, bleaching treatment was performed twice by mixing the suspension with a 8.5 g/L NaClO2 solution in sodium acetate buffer (pH 4.5) at 70 Ā°C for 2 h. The bleached cellulose was rinsed with distilled water until the pH remained stable. The puriļ¬ed bacterial cellulose was then hydrolyzed with 2.5 M HCl at 70 Ā°C for 2 h as described by Gilkes et al.33 Acid was removed by successive centrifugations during 10 min at 10 000g and redispersion of the solid materials in ultrapure water (18.2 MĪ©) up to pH 5. The suspension was further homogenized by ultrasound treatment for about 1 min (ultrasonic processor XL 2020, Misonix, Farmingdale, NY). The resulting 1% suspension was then extensively dialyzed against water to remove any remaining contaminants and deionized by mixing with mixed bed ion-exchange resin. For storage, one drop of CHCl3 per 250 mL was added to the suspension and kept at 4 Ā°C. 2.3. Transmission Electron Microscopy (TEM). A total of 20 Ī¼L of a BCN suspension in water (0.1% w/v) was deposited on a freshly glow-discharged carbon-coated electron microscope grid (200 mesh copper, Delta Microscopies, France) and the excess removed. Negative staining was performed by adding 20 Ī¼L of uranyl acetate solution (2% w/v). The excess solution was removed and the grids were dried in an oven at 40 Ā°C just before observation. The grid was observed under standard conditions with a JEOL JEM-1230 transmission electron microscope operating at 80 kV. 2.4. Emulsion Preparation and Characterization. Emulsion Preparation. The oil in water (o/w) emulsions were prepared using hexadecane and a BCN aqueous suspension at the required concentra- tion without further dilution. All the emulsions were prepared using an oil/aqueous phase ratio of 30/70. Practically, 0.3 mL of hexadecane was added to 0.7 mL of aqueous suspension in a plastic vial and sonicated with an ultrasonic device with a dipping titanium probe close to the surface (power level at 1.5 dial value corresponds to 2 W/mL applied power determined by heat balance), alternating 3 s sonication with a 3 s standby for 20 s. Stability Test. Stability of the generated emulsions was checked by centrifugation for 2 min at 4000g. The emulsion volume and drop size measured for various centrifugation times kept stable from 30 s to 40 min. Photographs of the vials containing the emulsions were taken with a P1 digital camera (Olympus), and the thickness of the creaming layer was measured with a digital caliper. Light Microscopy. The emulsions were all visualized by light micro- scopy. A total of 15 Ī¼L of the resulting Pickering emulsion was added to 1 mL of distilled water and stirred by vortex, then a single drop was poured onto a slide and observed via microscope (BX51 Olympus). Droplet diameter was measured by image analysis using the ā€œImageJā€ software and compared to the drop size distribution determined by laser light diffraction using a Malvern 2000 granulometer apparatus equipped with a HeNe laser (Malvern Instruments, U.K.) with Fraunhofer diffraction. The measurements were systematically carried out in tripli- cate. The diameter was expressed as surface mean diameter D(3,2) (the Sauter diameter), and eventual aggregation was checked by comparing these values with those where sodium dodecyl sulfate (SDS) was added just before measurement. Similar results were obtained via granulometer and ImageJ analysis. Sugar Analysis. In order to evaluate the amount of cellulose involved in the droplet stabilization, quantification of the cellulose released in the aqueous subphase after centrifugation was carried out by colorimetric titration after sulfuric acid degradation. Subphases were lyophilized, dispersed in 26 N sulfuric acid for 1 h at 25 Ā°C, and afterward hydrolyzed in 2 M sulfuric acid for 6 h at 100 Ā°C before colorimetric titration with orcinol sulfuric acid method with a Skalar autoanalyser. Glucose was used as a standard. 2.5. Confocal Laser Scanning Microscopy (CLSM). For CLSM visualization, the emulsions were prepared with double staining. Hexadecane and cellulose were stained with BODIPY (564/570) fluorophore andcalcofluor (347/450) respectively. Images were acquired using a Zeiss LSM 410 confocal microscope (Zeiss, Gottingen, Germany) using a x40 water-immersion lens with an optical section thickness around 2 Ī¼m. 2.6. Scanning Electron Microscopy (SEM). Because of hex- adecane volatility, the emulsions formed could not be introduced in the SEM chamber. The BCNs proved to stabilize the styrene/water interface and form a stable emulsion. This ability to form solid particles was then used to visualize the distribution of BCNs at the drop inter- face by SEM. Therefore, aqueous suspensions containing 0.5, 1, and 5 g/L BCNs were sonicated for 20 s and degassed with nitrogen for 10 min. Styrene was mixed with V65, an oil-soluble initiator, to obtain a
  • 4. 7473 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE styrene/V-65 ratio of 120/1 (w/w).14 A total of 86 Ī¼L of this mixture was added to 1.0 mL of the BCN suspension, and an emulsion was prepared by sonication for 20 s (3 s pulse on, alternating with 3 s pulse off). Then 500 Ī¼L of water was added to dilute the already formed Pickering droplets. After vortex mixing, the emulsions were again degassed with nitrogen gas for 10 min before polymerization at 63 Ā°C, without stirring, for 24 h. The dried beads were metallized with platinum and visualized with a JEOL 6400F instrument. 2.7. Coverage Determination. Coverage was determined from the amount of particles involved in the emulsion and the oil effectively trapped within the droplets. The absence of BCN in the nonemulsified aqueous phase after centrifugation was confirmed by sugar analysis after sulfuric hydrolysis. The surface coverage C is then given by the ratio of the theoretical maximum surface susceptible to be covered by the particles Sp and the total surface displayed by the oil droplets Sd: C Ā¼ Sp Sd Ć°1ƞ where Sp Ā¼ NpLl Ā¼ mp hFp Ć°2ƞ and Sd Ā¼ 4Ļ€R2 3Voil 4Ļ€R3 Ā¼ 3Voil R Ć°3ƞ where Np is the number of BCNs, L, l. and h are, respectively, the length, width, and thickness of BCN, mp is the mass of BCNs, Fp is the BCN density, R is the average drop radius, and Voil the volume of oil included in the emulsion after centrifugation. The total coverage can be expressed as C Ā¼ mpD 6hFVoil Ć°4ƞ where D is the D(3,2) average radius of the droplets. 3. RESULTS AND DISCUSSION 3.1. BCN Preparation. BCNs were isolated by acid hydrolysis to remove the amorphous part of the microfibrils and then dispersed using a sonication device. Bacterial cellulose hydrolysis is generally performed with sulfuric acid which leads to charged particles,34 whereas hydrolysis with hydrochloric acid results in slightly carboxylated surfaces.35 The nanocrystals generated by sulfuric or hydrochloric hydrolysis have rectangular cross sec- tions or a ribbonlike shape with dimensions of ca. 10 nm 50 nm and range in length from 100 nm to several micrometers, with these dimensions depending on the hydrolysis conditions.34,36 The bacterial cellulose used in this work was hydrolyzed with hydrochloric acid. At the end of the process, the sample charge density was measured by conductometric titration (see the Supporting Information). This titration revealed a low level of residual charges, involving weak charge groups such as carboxylic groups, below 103 e/nm2 . TEM images of the suspension showed that the crystalline particles were fairly homogeneous, despite a tendency to aggregate due to the absence of repulsive surface charges (Figure 1). This aggregation is not observed with sulfated cellulosic nanoparticles such as cotton whiskers.31 Analysis of the TEM images using ImageJ software indicated an average length of 855 nm and width of 17 nm. A thickness of 7 nm was determined by atomic force microscopy (AFM) (see the Supporting Information). These data are in accordance with most other authors who reported sizes for the individual nanocrystals from bacterial cellulose thickness ca. 510 nm and length from 100 to 1000 nm for acid-treated samples37,38 whereas the reported width ranged from 5 to 50 nm.35,37 As a result, the particles produced show crystalline, elongated, sub- micrometer sized characteristics. 3.2. Emulsion Preparation. The aqueous phase, for all tested emulsions, consisted of cellulosic nanocrystalline particles dis- persed in water at the required concentration without further treatment. Hexadecane was added afterward. The biphasic system was then sonicated, resulting in a very stable oil in water emulsion. Respective localization of the nanocrystals at the oil interface and ordering of the dropletā€™s surface was checked by CLSM and SEM. Calcoļ¬‚uor was used as ļ¬‚uorochrome for cellulosic materi- al, while BODIPY presenting aļ¬ƒnity for hydrophobic liquids was dissolved in the oil phase. This double staining allows one to clearly distinguish the inner oily phase and the surface covered by cellulosic particles (Figure 2a). Surface organization was exam- ined in detail by SEM visualization of the individual droplets. Although cryo SEM would allow direct observation of oil in water Pickering emulsions,39 polymerizable resins oļ¬€er convenient alternatives for oil in water emulsion using the classical SEM approach. Bon and Colver prepared latex particles using Lapo- nite clay discs as stabilizers, with the inner part being polymerized from a variety of hydrophobic monomers.14 BCNs showed the same ability to stabilize styrene and hexadecane droplets, and therefore, styrene was selected. An aqueous BCN suspension was then mixed with styrene, emulsiļ¬ed using the same above- described emulsifying protocol, and visualized (Figure 2b). Despite this process being diļ¬€erent from the hexadecane one, involving styrene, the BCNs displayed analogous interfacial pro- perties for the styrene/water emulsion and a hexadecane/water Figure 1. BCN morphology by TEM of a negatively stained dilute suspension of BCN.
  • 5. 7474 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE emulsion. The polymerization step served just as a ļ¬xing step of the beads formed. We therefore assumed that the resulting emulsion was representative of the present studied system. Several very small noncovered white beads (diameter of the beads was generally below 100 nm) were observed for all the samples. These were artifactual outgrowths formed during styrene polymerization. SEM images showed that the BCN nanoparticles were evenly distributed at the surface and bent to follow the curvation of each droplet. It means that the cellulosic nanocrystals when wetted by the hydrophobic phase present enough ļ¬‚exibility to bend along the surface. In other words, the tension required for droplet formation is high enough to force these colloidal particles to align without desorbing them. We can assume that they will align preferentially according to the face presenting the lower thickness which is 7 nm. 3.3. Emulsion Stability. Pickering emulsions were formulated at a 30/70 ratio (o/w), with a 5 g/L suspension of BCN in the water phase. These conditions were used to test stability under various temperature conditions. Very high stability was observed, without change in droplet size, even under various mechanical treatments of the cream layer such as vortex or rotor stator blender at 15 000 rpm. No variation in droplet size was also observed after centrifugation or after keeping the samples for 1 month at 4 Ā°C, at 40 Ā°C or up to 2 h at 80 Ā°C. These various tests even after dilution were performed over months. The absence of drop size variation in these conditions consolidates the fact that irreversible adsorption occurs; indeed desorp- tion might lead to phase separation, and this has never been observed. Further tests were then carried out to specify stability characteristics. An emulsion is commonly considered stable if it is resistant to physical changes over a practical length of time. It can be tested by several methods including centrifugation, ļ¬ltration, shaking or stirring, low intensity ultrasonic vibrations, or heating. All the listed methods used for emulsion destabilization induce mostly creaming or sedimentation, ļ¬‚occulation, and eventually coalescence. Concretely, creaming forces contact (collision and sticking) between the droplets and allows coalescence to occur whereby the majority of the droplets merge creating fewer larger droplets, thereby reducing the total interface area of the system. As hexadecane has a lower density than water (d = 0.82 g/mL at 25 Ā°C), a creaming process was always observed. However an emulsion can be considered stable as long as no coalescence occurs; that is, the size and size distribution should not change. When the emulsions were characterized over time, a stable drop size was observed for several months although natural creaming occurred. Centrifugation accelerates the creaming process, forcing the droplets to concentrate. The excess water is then excluded from the emulsion, leading to close packing conditions. Centrifugation at 4000g was considered suitable for following the resistance of droplets to coalescence. Two parameters were used to characterize and evaluate the stability of the resulting emul- sions: (i) the average drop size obtained after dispersion of a few microliters of the cream in water and (ii) the volume of the emulsion after centrifugation. The ability of BCNs to stabilize the droplets was assessed by varying the concentration of nanocrystals in the aqueous suspen- sion from 0 to 5 g/L. Before centrifugation, the emulsion volume increased regularly with the amount of BCN added, for a ļ¬xed oil content (Figure 3). This indicated that trapping of the aqueous phase was increased when a larger amount of BCNs was present. After centrifugation at 4000g, the emulsion with concentrations below 2 g/L of BCNs ā€œbroke upā€, and the emulsion volume could no longer be measured. For concentrations above 2 g/L of BCNs, dense white emulsions were obtained that resisted to the stress induced by centrifugation. The emulsion ratios, deļ¬ned as the volume of oil over the volume of emulsion, were calculated and are shown in Figure 4. At BCN concentrations below 2 g/L, the oil and water phases separate and coalescence occurs by compression during the centrifugation process. At higher BCN concentrations, the percentage of oil trapped into the emulsion increases sharply to reach a plateau value of around 0.7. This value is worth noting, as it is close to the theoretical close packing condition of 0.74 for monodispersed spheres. It is worth noting that the same limit was observed whatever the centrifugation speed at 4000g and 10 000g, leading to the same packing conditions whatever the BCN concentration. These droplets, that are resistant to cen- trifugation, can also be dispersed in water and shaken without disruption. The centrifugation deformed the droplets and ex- cluded the water layers present at the interface without breaking the droplets. The total volume of oil remained trapped within the emulsion, with no modiļ¬cation of emulsion volume whatever the concentration of BCN used, when centrifugation was stopped, that is, after relaxation of the droplets. Above 2 g/L, the emulsions displayed excellent mechanical resistance toward deformation and coalescence. 3.4. Droplet Characterization. Droplet size variations were monitored by measuring the surface mean diameter D(3,2) and varying concentrations of BCN in the water phase for a fixed amount of oil. Results are given for a ratio of 30/70 (o/w) (Figure 5). Droplet size showed a clear tendency to coalescence at the lowest concentrations of BCN. Then sizes decreased to a plateau Figure 2. Surface contribution of BCN. (a) Confocal laser scanning micrograph of droplets stabilized by BCN with double staining (hexadecane phase stained with BODIPY564/570, BCN stained with calcoļ¬‚uor). (b and c) Scanning electron micrographs of styrene Pickering emulsion stabilized by BCN and polymerized using V65 initiator.
  • 6. 7475 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE value of 4.2 Ī¼m diameter for all emulsions containing more than 2 g/L of BCNs in the water phase. The upper image in Figure 3 taken before centrifugation showed that the emulsion volume increased regularly with the amount of BCNs. Below 2 g/L, the increasing amount of BCN particles resulted in decreasing average droplet size which led to a larger interfacial area and thus to a higher emulsion volume. Similar coalescence tendency has been previously reported for other types of Pickering emulsions.3,7,40 The method chosen to obtain our emulsions is based on a limited coalescence41,40 process for the samples prepared with the lowest BCN concentrations and up to 2 g/L. This occurs when sonication produces a much larger area of the oil/water interface than can potentially be covered by the nanocrystals. When sonication is stopped, the partially unprotected droplets coalesce. This coalescence results in a decrease of the oil/water interface and stops as soon as the interface is suļ¬ƒciently covered. For the samples prepared with the highest BCN concentrations, at and above 2 g/L, a strong emulsion of stable droplet diameter around 4 Ī¼m was obtained, irrespective of the amount of particles added, which was resistant to deformation. The drop size limit has rarely been discussed in literature. One argument comparing the drop size according to the surface chemistry of the nano- particles was analyzed in terms of emulsion stability. It was observed that the droplets were smaller when more stable emulsion conditions were used.9,42 In the present study, the sonication process involved a rather high energy input with production of submicrometer size droplets and the stability of BCNs at the interface was signiļ¬cant. The size limitation might therefore be due to the size and ļ¬‚exibility of the solid particles. Indeed, BCNs consist of crystalline particles 855 nm in length, and the size of the particles might be correlated to the droplet size. No conclusions can be drawn from the present results, but diļ¬€erent nanocrystal shapes can be produced according to the cellulosic origin. The comparisons should be performed with particles diļ¬€ering in morphology to validate this assumption. 3.5. Evaluation of Coverage. In order to check that the particles had been irreversibly adsorbed at the o/w interface, the particles remaining in the aqueous subphase after emulsification and centrifugation were quantified by determining the sugar content. No or negligible amounts of BCNs were found outside the emulsion (data not shown) which meant that all the particles introduced were involved in the emulsion, at the concentration range under study. A relationship between the mass of solid particles (mp) and the average droplet diameter (D) has already been proposed.16 According to the equations proposed in section 2, the ļ¬nal interfacial area should be controlled by mp. The average droplet diameter (D) should then be inversely proportional to the amount of solid particles included (mp): 1 D Ā¼ mp 6hVdC Ć°5ƞ where C is the surface coverage, that is, the percentage of droplet surface area covered by cellulosic particle, h is the thickness of the BCN covering layer (7 nm for a monolayer), and Vd is the total volume of the dispersed phase. The evolution of the inverse diameter (1/D) for the various amounts of BCNs introduced showed a linear increase, followed by stabilization at the higher concentrations (Figure 6). The ļ¬rst part of the plot increased linearly over the lower concentrations, showing the same mode of coverage for all the emulsions. This was observed up to a critical concentration deļ¬ned by the deviation to linear mode in Figure 6. The tendency to plateau shown by the second part of the curve would indicate changes in the coverage arrangement. These results indicate that when a limited amount of BCNs is introduced, compared to the oil volume present, individual droplets are produced for which the diameter is determined by the amount of stabilizing particles available according to the limited coalescence process. The coalescence process was Figure 4. Ratio of hexadecane in the emulsions (v/v) measured after centrifugation at 4000g for increasing BCN concentrations in the water phase (g/L). The line serves to guide the eyes. Figure 3. Hexadecane/aqueous BCN o/w emulsion stability (a) before centrifugation and (b) after centrifugation at 4000g for increasing BCN concentration in the water phase from 0.1 to 5 g/L.
  • 7. 7476 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE observed up to a critical amount of 5.2 mg of BCNn added to the water phase to stabilize 1 mL of hexadecane to produce the droplet diameter of 4.2 Ī¼m. It corresponded to a concentration of 2.2 g/L BCNn in the water phase as previously deļ¬ned. Above this concentration, more and more nanocrystals can be added without changing the droplet diameter. Cellulosic ma- terials are known to aggregate in the aqueous phase via van der Waals interactions and hydrogen bonding. The induced over- load of material might result in ļ¬‚occulation due to particles nonadsorbed or only partially adsorbed at the interface. This would produce interconnected particles and change BCN organization at the surface of the droplets resulting in the slope variation. Interface organization was investigated by calculating the surface coverage according to eq 4, for emulsions prepared with diļ¬€erent BCN concentrations. These values were then plotted against mp, that is, the mass of BCN in the aqueous phase, as shown in Figure 7, to characterize the packing density of the BCN particles at the interface. At low concentrations, the few droplets showed identical coverage up to 5.2 mg BCN/ mL hexadecane, the minimum required for stable droplets having 60% coverage. After that, the percentage coverage Figure 5. Droplet size dependence on BCN content (upper ļ¬gure) for droplet diameters D(3,2) vs BCN concentration in the water phase in an emulsion containing hexadecane with a 30/70 oil/water ratio. (lower images) Transmission optical micrographs of the same emulsions; the corresponding concentrations are given in the images. Figure 6. Limited coalescence process visualized by the inverse D(3,2) diameter plotted against the amount of particles included in the water phase per milliliter of hexadecane. Figure 7. Evolution of coverage vs the amount of particles included in the water phase per milliliter of hexadecane for a 30/70 (o/w) ratio.
  • 8. 7477 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE increased to 100% for the highest BCN concentration tested, that is, nearly 12 mg/mL hexadecane (which corresponds to a suspension of 5 g/L BCN). This 60% coverage value is not surprising, as values ranging from 22% to 70% have been reported in the literature for other Pickering systems;40,43 even a value as low as 8% was deļ¬ned for concentrated latex micrometer-sized particles stabilized by nanosized spherical silica particles.16 This coverage is deļ¬ned as the ratio of the area which could be covered by the particles (length width amount of particles) and the calculated total area of the oil droplets, taking into account the D(3,2) drop diameter measured for each emulsion of varying BCN concentration. The average BCN dimensions of individual nanocrystals are used, measured by TEM and AFM microscopies, without taking into account possible aggregation. We can therefore assume that the measured available nanocrystal surface and consequently the calculated coverage are overesti- mates compared to the truly available area. As the particles are irreversibly adsorbed at the interface and the principle of Pickering stabilization results in partial wetting adsorption, the formation of multilayers was unlikely. However, above 5.2 mg/mL hexadecane, the percentage coverage increased to even more than 100%. This could be attributed to the shape of the particles, the elongated form and relative ļ¬‚exibility at the surface leading to overlapping of the particles at high concentra- tions. Thus, a simple geometric approach presents a limitation to describe the BCN coverage properties due its intrinsic morpho- logical and associative characteristics. This was checked by SEM visualization of the droplet surface prepared by using BCN concentrations of 0.5, 1, and 5 g/L. Figure 8 shows SEM images of the polystyrene droplets covered by nanocrystals. Comparison of the diļ¬€erent preparations revealed that, whatever the amount of BCN introduced, the nanocrystals bent along the beads, overlapping one over each other and eventually forming long ļ¬bers. The tendency to aggregate inherent to the uncharged BCN nanostructure was observed even at the lowest concentration. However, coverage was lower for the emulsion prepared with the 0.5 g/L suspension, and greater overlapping of particles was observed with the 5 g/L suspension. Several papers highlighted the outstanding stabilizing proper- ties of rodlike particles,26,44,45 and BCNs are generally assumed to be rigid crystals with a high aspect ratio but their thickness of 7 nm allows a certain ļ¬‚exibility when aligned along the droplet interface. We therefore never observed any ā€œnestlikeā€ structures as obtained for very rigid particles such as CaCO3.46 Finally, if this ļ¬‚exibility is the limitation point, the plateau observed for droplet size around 4 Ī¼m in diameter might be correlated with this ability of the BCNs to bend. As a result, it would also be the main explanation to the break point observed in Figure 6. Once the maximum curvature of the particles is reached, the interface area is ļ¬xed and adding BCNs induces a new coverage organiza- tion. However, if the strength necessary to stay bent at the interface becomes high, the particles might then desorb from the interface while we observed a very high stability of these drops. The BCNs present the particularity to self-associate, and what- ever the concentration a more or less densely packed 2D network forms at the surface of the droplets. This network is highly stable both because the energy of adsorption prevents the particles from being removed from the interface and because particle aggregation prevents coalescence. Steric hindrance appears to be the major mechanism responsible for droplet stability.47 The strongadhesionofparticlestothe interfaceconfers to the emulsion high resistance to coalescence and high stability. This has to be attributed to the particular behavior of cellulosic derivatives, that is, their elongated shape and the low charged surface chemistry forming an entangled network of isolated nanocrystals. ConsideringBCNs themselves, these quasi-neutral particles are generally considered as hydrophilic matter, but they can stabilize at the oil/water interface. Being regular crystalline particles, they are organized according to various crystalline plans and some of these plans expose a more hydrophobic surface.48 When well oriented, this may promote the particle interfacial properties. As a result, the BCNs prepared present both hydrophilic and hydro- phobic characters in a good ratio. Indeed, with higher surface charged density, they do not stabilize emulsions because their too high aļ¬ƒnity for the aqueous phase prevents stabilization at the o/w interface. On the other hand, the absence of charge would induce formation of big aggregates unable to form individual Figure 8. SEM images for metallization of a polymerized styrene/water emulsion stabilized by BCN suspensions, from left to right, at 0.5, 1, and 5 g/L.
  • 9. 7478 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE droplets. Contact angle determination is diļ¬ƒcult to conduct at the liquid ļ¬‚uid interface; however, some methods such as the one developed by Paunov49 might help to understand the attachment of the particles to the interface. As a result, bearing no chemical function and resisting to high acid hydrolysis, the present BCNs allow droplet stabilization over a large domain of pH, time, and temperature. Bacterial cellulose nanocrystals present, for example, an aspect ratio signiļ¬cantly larger than that of wood and cotton nanocrystals.34 For further emulsion studies, it is known that cel- lulosic nanoparticles varying in shape (length and aspect ratios) can be produced according to the cellulose origin (cotton, algae, animal) or after treatments such as recrystallization (regenerated cellulose II). From the literature, various lengths can be obtained from some tens of nanometers to several micrometers. Since the coverage organization can be modiļ¬ed by the crystal morphol- ogy, we can expect variations in the emulsion characteristics particularly from the curvature adaptability and networking aptitude. Their shape versatility and high stability added to their biorenewable property as raw material make the present BCNs or other cellulosic derivatives outstanding sources for study of the Pickering interfacial stabilization process and large application domains such as for cosmetic, medical, or food industry notably. 4. CONCLUSIONS Bacterial cellulosic nanocrystals were produced by hydrochlo- ric acid hydrolysis and resulted in nanoparticles of very low charge density. After sonication, they resulted in a suspension stable for several months. This process provided nanosized cellulosic particles which were directly able to stabilize irrever- sibly an oil in water Pickering emulsion. BCNs can therefore be used to prepare a monodispersed emulsion without any further modiļ¬cation or wrapping process. The emulsions produced have been characterized and proved to be stable over months whatever the BCN concentration as long as no centrifugation was performed. However, above a limit evaluated at 5.2 mg of BCN to stabilize 1 mL of hexadecane, an emulsion able to be dispersed in water and resistant to centrifu- gation at 4000g was obtained. Studies varying the amounts of nanoparticles were carried out to investigate the surface organization of the droplets stabilized by BCNs. At the lowest concentrations, limited coalescence occurred and the droplet size decreased up to about 4 Ī¼m diameter. Droplets with a constant surface coverage of 60% were formed, which represents for our system the minimum required tostabilize the emulsion. When more than 5.2 mg of BCN/mL of hexadecane was introduced, the BCN particles were in excess and presented a much greater available surface area than was required to stabilize 4 Ī¼m diameter droplets. The surface coverage increased toward 100% as the amounts of added BCN were increased. However, no BCN was found in the aqueous phase after centrifugation. We propose that irreversible adsorption of the particles, associated with steric hindrance of the 2D network formed, at the interface was responsible for the very high droplet stability obtained. ā€™ ASSOCIATED CONTENT b S Supporting Information. Additionnal results about the BCN surface charge density by conductometric titration and thickness by AFM determination. This material is available free of charge via the Internet at http://pubs.acs.org. ā€™ AUTHOR INFORMATION Corresponding Author *E-mail: capron@nantes.inra.fr. Telephone: 33(0)240675095. ā€™ ACKNOWLEDGMENT The authors thank Brigitte Bouchet for assistance in TEM experiments (BIBS platform, INRA Nantes, France), Nicolas Stephan for assistance in SEM experiments (IMN, Nantes, France), Patricia Bertoncini for AFM measurements, Solene Grosbois for excellent technical assistance, and R egion Pays de la Loire (RMB network) for ļ¬nancial support. ā€™ REFERENCES (1) Ramsden, W. Proc. R. Soc. 1903, 72, 156. (2) Pickering, S. U. J. Chem. Soc. 1907, 91, 2001. (3) Tambe, E. T.; Sharma, M. M. J. Colloid Interface Sci. 1993, 157, 244ā€“253. (4) Binks, B. P.; Lumsdon, S. O. Langmuir 2001, 17, 4540ā€“4547. (5) Pieranski, P. Phys. Rev. Lett. 1980, 45, 569ā€“572. (6) Binks, B. P. Curr. Opin. Colloid Interface Sci. 2002, 7, 21ā€“41. (7) Aveyard, R.; Binks, B. P.; Clint, J. H. Adv. Colloid Interface Sci. 2003, 100, 503ā€“546. (8) Finkle, P.; Draper, H. D.; H., H. J. J. Am. Chem. Soc. 1923, 45, 2780ā€“2788. (9) Binks, B. P.; Lumsdon, S. O. Langmuir 2000, 16, 8622ā€“8631. (10) Binks, B. P.; Philip, J.; Rodrigues, J. A. Langmuir 2005, 21, 3296ā€“3302. (11) Midmore, B. R. Colloids Surf., A 1998, 132, 257ā€“265. (12) Colard, C. A. L.; Teixeira, R. F. A.; Bon, S. A. F. Langmuir 2010, 26, 7915ā€“7921. (13) Tsugita, A.; Takemoto, S.; Mori, K.; Yoneya, T.; Otani, Y. J. Colloid Interface Sci. 1983, 95, 551ā€“560. (14) Bon, S. A. F.; Colver, P. J. Langmuir 2007, 23, 8316ā€“8322. (15) Cui, Z. G.; Shi, K. Z.; Cui, Y. Z.; Binks, B. P. Colloids Surf., A 2008, 329, 67ā€“74. (16) Gautier, F.; Destribats, M.; Perrier-Cornet, R.; Dechezelles, J. F.; Giermanska, J.; Heroguez, V.; Ravaine, S.; Leal-Calderon, F.; Schmitt, V. Phys. Chem. Chem. Phys. 2007, 9, 6455ā€“6462. (17) Grosse, I.; Estel, K. Colloid Polym. Sci. 2000, 278, 1000ā€“1006. (18) Binks, B. P.; Rodrigues, J. A.; Frith, W. J. Langmuir 2007, 23, 3626ā€“3636. (19) Ougiya, H.; Watanabe, K.; Morinaga, Y.; Yoshinaga, F. Biosci., Biotechnol., Biochem. 1997, 61, 1541ā€“1545. (20) Blaker, J. J.; Lee, K. Y.; Li, X. X.; Menner, A.; Bismarck, A. Green Chem. 2009, 11, 1321ā€“1326. (21) Yusoļ¬€, A.; Murray, B. S. Food Hydrocolloids 2011, 25, 42ā€“55. (22) French, A. D.; Bertoniere, N. R.; Brown, R. M.; Chanzy, H.; Gray, D. G.; Hattori, K.; Glasser, W. G. In Encyclopedia of Polymer Science and Technology, 3rd ed.; Kroschwitz, J. I., Ed.; John Wiley Sons: New York, 2003; pp 473507. (23) Rowland, S. P.; Roberts, E. J. J. Polym. Sci., Part A: Polym. Chem. 1972, 10, 867ā€“879. (24) Eichhorn, S. J.; Dufresne, A.; Aranguren, M.; Marcovich, N. E.; Capadona, J. R.; Rowan, S. J.; Weder, C.; Thielemans, W.; Roman, M.; Renneckar, S.; Gindl, W.; Veigel, S.; Keckes, J.; Yano, H.; Abe, K.; Nogi, M.; Nakagaito, A. N.; Mangalam, A.; Simonsen, J.; Benight, A. S.; Bismarck, A.; Berglund, L. A.; Peijs, T. J. Mater. Sci. 2010, 45, 1ā€“33. (25) Oza, K. P.; Frank, S. G. J. Dispersion Sci. Technol. 1986, 7, 543ā€“561. (26) Wege, H. A.; Kim, S.; Paunov, V. N.; Zhong, Q. X.; Velev, O. D. Langmuir 2008, 24, 9245ā€“9253. (27) Jonoobi, M.; Harun, J.; Mathew, A. P.; Hussein, M. Z. B.; Oksman, K. Cellulose 2010, 17, 299ā€“307.
  • 10. 7479 dx.doi.org/10.1021/la200971f |Langmuir 2011, 27, 7471ā€“7479 Langmuir ARTICLE (28) Andresen, M.; Stenius, P. J. Dispersion Sci. Technol. 2007, 28, 837ā€“844. (29) Wagberg, L.; Decher, G.; Norgren, M.; Lindstrom, T.; Ankerfors, M.; Axnas, K. Langmuir 2008, 24, 784ā€“795. (30) Ranby, B. G. Discuss. Faraday Soc. 1951, 11, 158ā€“164. (31) Elazzouzi-Hafraoui, S.; Nishiyama, Y.; Putaux, J. L.; Heux, L.; Dubreuil, F.; Rochas, C. Biomacromolecules 2008, 9, 57ā€“65. (32) Samir, M.; Alloin, F.; Dufresne, A. Biomacromolecules 2005, 6, 612ā€“626. (33) Gilkes, N. R.; Jervis, E.; Henrissat, B.; Tekant, B.; Miller, R. C.; Warren, R. A. J.; Kilburn, D. G. J. Biol. Chem. 1992, 267, 6743ā€“6749. (34) Araki, J.; Kuga, S. Langmuir 2001, 17, 4493ā€“4496. (35) Araki, J.; Wada, M.; Kuga, S.; Okano, T. Colloids Surf., A 1998, 142, 75ā€“82. (36) Hirai, A.; Inui, O.; Horii, F.; Tsuji, M. Langmuir 2009, 25, 497ā€“502. (37) Grunert, M.; Winter, W. T. J. Polym. Environ. 2002, 10, 27ā€“30. (38) Habibi, Y.; Lucia, L. A.; Rojas, O. J. Chem. Rev. 2010, 110, 3479ā€“3500. (39) Haase, M. F.; Grigoriev, D.; Moehwald, H.; Tiersch, B.; Shchukin, D. G. Langmuir 2011, 27, 74ā€“82. (40) Arditty, S.; Whitby, C. P.; Binks, B. P.; Schmitt, V.; Leal-Calderon, F. Eur. Phys. J. E 2003, 12, 355ā€“355. (41) Whitesides, T. H.; Ross, D. S. J. Colloid Interface Sci. 1995, 169, 48ā€“59. (42) Frelichowska, J.; Bolzinger, M. A.; Chevalier, Y. J. Colloid Interface Sci. 2010, 351, 348ā€“356. (43) Nie, Z. H.; Il Park, J.; Li, W.; Bon, S. A. F.; Kumacheva, E. J. Am. Chem. Soc. 2008, 130, 16508ā€“16509. (44) Madivala, B.; Vandebril, S.; Fransaer, J.; Vermant, J. Soft Matter 2009, 5, 1717ā€“1727. (45) Alargova, R. G.; Warhadpande, D. S.; Paunov, V. N.; Velev, O. D. Langmuir 2004, 20, 10371ā€“10374. (46) Zhou, W. Z.; Cao, J.; Liu, W. C.; Stoyanov, S. Angew. Chem., Int. Ed. 2009, 48, 378ā€“381. (47) Lopetinsky, R.; Masliyah, J.; Zhenghe, X. Solid stabilized emulsion: A review. In Colloidal particles at liquid interfaces; Binks, B. P., Horozov, T. S., Eds.; Cambridge University Press: Cambridge, 2006; Vol. Chap. 6, pp 185224. (48) Mazeau, K.; Rivet, A. Biomacromolecules 2008, 9, 1352ā€“1354. (49) Paunov, V. N. Langmuir 2003, 19, 7970ā€“7976. View publication stats View publication stats