Facile Synthesis of Nanocapsules and Hollow Nanoparticles Consisting of Fluorinated Polymer Shells...
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Facile Synthesis of Nanocapsules and HollowNanoparticles Consisting of FluorinatedPolymer Shells by Interfacial RAFTMiniemulsion Polymerization
Hao Chen, Yingwu Luo*
Nanocapsulesmade of a cross-linked poly(dodecafluoroheptyl acrylate) shell were successfullysynthesized by interfacial RAFT miniemulsion polymerization. The well-defined hollowfluorinated polymer structures were obtained by the subsequent removal of the liquid corematerials. The core/shell ratio could be easily tuned up to 1:1 by changing the conditions. Inthe cases of high core/shell ratio of 1:2 and 1:1, the nanocapsules were severely deformed,which was improved by increasing the cross-linker amount up to 30wt.-%. It was concludedthat the utility of the interfacial RAFTminiemulsion polymerization overcamethe thermodynamic and kinetic barriersin a conventional miniemulsion polymeri-zation.
Introduction
In the past decades, synthesis of polymer nanocapsules of
active substance or hollow polymer nanoparticles has
received tremendous attentions due to their potential
applications in many emerging fields like drug delivery,[1]
dye encapsulation,[2] catalysis,[3] and biomaterial sensor.[4]
Many kinds of polymers such as polyelectrolytes,[5,6]
polystyrene,[7–9] poly(butyl acrylate),[10] poly(L-lactide),
polycaprolactone/poly(ethylene oxide) block copoly-
mers,[11] and polyethylcyanoacrylate[12] were used as
polymer shell of nanocapsules for entrapping different
materials in core. Due to the strongest C–F single bonds
among organic molecules, low polarity, and good coverage
of polymermain carbon chains, fluorinated polymers show
many unique properties like low refractive index, high
H. Chen, Y. LuoThe State Key Laboratory of Chemical Engineering, Department ofChemical and Biochemical Engineering, Zhejiang University,Hangzhou 310027, ChinaFax: þ86 571 8795 1612; E-mail: [email protected]
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oxygen andCO2 permeation, low surface energy,water and
oil repellence, chemical and thermal stability.[13–15] Nano-
capsules or nanoparticles with fluorinated polymer shells
would be of interest in many applications such as use as
oxygen carrier,[16] membranes for fuel cells, etc.[17,18]
However, to our best knowledge, there are no reports on
the synthesis of nanocapsules and hollow nanoparticles
with fluorinated polymer shells.
Manynovel techniqueshavebeen invented tosynthesize
polymernanocapsules orhollowstructures. Representative
techniques include block copolymers self-assembly in
selective solvents,[19–25] miniemulsion polymeriza-
tion,[8,9,26–28] and template methods such as layer-by-layer
assembly of inorganic silica on particles,[29] deposition on
mini-droplets,[30] or surface polymerization on nanoparti-
cles.[31] Among these techniques,miniemulsion polymeriza-
tion, particularly the interfacial reversible addition/
fragmentation chain-transfer (RAFT) miniemulsion poly-
merization, presents a convenient, green, highly efficient,
andscalableversatileapproach.[8,9]Astablefluorinated latex
has been successfully achieved by miniemulsion copoly-
merization of fluorinated (meth)acrylate and styrene/
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H. Chen, Y. Luo
methacrylate/acrylic acid using sodium dodecylsulfate
(SDS) as surfactant.[32] Compared with the emulsion
polymerization, the monomer transport problem of fluori-
nated monomer can be solved by the direct conversion of
monomer droplets into the particles in miniemulsion
polymerization, where monomer is in the pre-emulsified
minidroplets of about 100nm in diameter before initiating
the polymerization. In a miniemulsion polymerization,
nanoencapsulationof a liquid substance is fulfilled through
phase separationwithin the particles,which is triggered by
the polymerization.[28] Polymer nanocapsules of the liquid
substance are only formed when the polymer shell is more
hydrophilic than the corematerials and the polymer chains
newly created in the aqueous phase can transport to the
particle surface before precipitation.[28] Considering the
superhydrophobic nature of most fluorinated polymer, the
formation of the fluorinated polymer shell is particularly
difficult, according toTorza andMason[33] andSundberg.[34]
On the other hand, the cross-linked polymer shell is also
difficult to achieve since the cross-linked polymer clusters
are difficult to move to the surface of particles.[28]
Beinga typeof controlled/living radical polymerizations,
RAFT polymerization has been extensively investigated in
the past decade.[35,36] Using RAFT polymerization, the
synthesis of well-defined polymers with a low polydisper-
sity index (PDI),[37] block copolymers,[38] and gradient
polymers with controlled compositional profile along the
polymer chains,[39] and polymer brushes grafted on a
surface[40] has been achieved. More recently, an interfa-
cially-confined RAFT miniemulsion polymerization pro-
cess, which was constructed by using an amphiphilic
oligomeric RAFT agent as surfactant, was demonstrated to
be a straightforward route to synthesize the nanocap-
sules.[8,9] In the process, the amphiphilic oligomer RAFT
agent molecules initially anchored at the interface of oil or
particles would grow gradually in a living manner during
the polymerization course, leading to the in situ formation
of polymeric shell.[8,9] The nanocapsules of polystyrene
surrounding hexadecane core have been successfully
synthesized with different amphiphilic oligomeric RAFT
agents.[8,27,41] Here we report the well-defined nanocap-
sules and hollow nanoparticles with the cross-linked
fluorinated polymer shell, which cannot be obtained by
the conventional miniemulsion polymerization, can be
synthesized by the RAFT interfacial miniemulsion poly-
merization.
Scheme 1. Reactions to synthesize the amphi-RAFT agent.
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Experimental Part
Materials
Dodecafluoroheptyl acrylate [DFHA, (CF3)2CFCFHCF(CF3)CH2OOCC¼CH2], purchased from Xeogia Fluorine-Silicone Chemicals (Harbin,
China), and methacrylic acid [MAA, analytic reagent (AR)] were
purified by distillation under reduced pressure to remove inhibitor
before use. 4-Cyano-4(dodecylsulfanylthiocarbonyl)sulfanylpen-
tanoic acid (CDPA), as the initial RAFT agent, was synthesized and
purified as described in the literature.[42] 2,2’-Azoisobutyronitrile
(AIBN) as an initiator for miniemulsion polymerization was re-
crystallized twice from methanol. Divinylbenzene (mixture of
isomers, 80%) purchased from J&KChemical Ltd. waswashedwith
an aqueous solution of 10wt.-% sodiumhydroxide and then rinsed
withde-ionizedwater to remove inhibitorbeforeuse. 4,4’-Azobis(4-
cyano-pentanoic acid) (V501, initiator for the solution polymeriza-
tion, 99%, from Aldrich), dioxane (>99%, AR), hexane (AR),
tetrahydrofuran (THF, AR), sodium hydroxide (NaOH, AR), hydro-
chlorie acid (>99%), hexadecane (HD, 99%, from Alfa Aesar), hexyl
acetate (HA, Aladdin), sodium nitrite(>96%, AR), and SDS (96%)
were used without further purification.
Synthesis of the Amphiphilic Poly(MAA-co-DFHA)RAFT Agent
The amphiphilic poly(MAA-co-DFHA) RAFT agent (amphi-RAFT)
was synthesizedvia the solutionpolymerizationofMAAandDFHA
mediated by the small RAFT agent CDPA, as seen in Scheme 1. The
small RAFT agent CDPA (2 g, 4.96mmol), the initiator V501 (0.21 g,
0.71mmol), and fluorine-monomer DFHA (17.2 g, 44.56mmol),
MAA (7.88 g, 91.6mmol) were mixed and dissolved in dioxane
(40.7 g, solvent with small transfer coefficient). The solution was
introduced into a 150mL four-necked round flask. After N2
bubbling for 30min, the polymerization proceeded with magne-
tically stirring for 8 h at 80 8C. The product (amphi-RAFT) of yellow
solid powderwas then collected by precipitating the solution three
timeswith icy hexane and then dried in a vacuumoven at 30 8C for
3 h. The overall monomer conversion from gravimetric analysis
was about 35%.
1H NMR Analysis
The structure of the amphi-RAFT agent was determined by Bruker
Avance DMX 500MHz spectrometer with DMSO-d6 as NMR
solvent. The 1H NMR spectrum of the amphi-RAFT is shown in
Figure 1 including signal assignment. From the spectrum, it was
estimated using Equation (1) and (2) that each amphi-RAFT agent
moleculehad7.0MAAunits and2.1DFHAunits,whichagreedwell
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Figure 1. 1H NMR spectrum of the amphi-RAFT agent recorded inDMSO-d6.
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with the conversion data,
Tab
Ru
Exp
Exp
Exp
Exp
Exp
a)Weig
www.M
NMAA ¼ I�COOH�0:5I�CH2�COOH
0:5I�CH2�COOH(1)
NDFHA ¼ I�CHF�0:5I�CH2�COOH
(2)
whereNMAA is the number ofMAA unit in each amphi-RAFT agent
molecule; NDFHA is the number of DFHA unit in each amphi-RAFT
agent molecule; I–COOH is the integral area of the peak at d¼ 12.4,
I�CH2�COOH is the integral area of the peak at d¼2.3, and I–CHF– is
the integral area of the peak at d¼6.4. The reactivity ratios ofMAA
and DFHA were not available in the literature. Due to the
structural similarity, the reactivity ratios of MAA and butyl
acrylate (rMAA/BA¼1.31, rBA/MAA¼ 0.35[43]) was used to calculate
the theoretical copolymer composition by Mayo-Lewis equa-
tion[44] and the result was also in good agreement with 1H NMR
data.
le 1. Recipe for the synthesis of cross-linked fluorinated polymer
n AIBN Total monomers Core/shell
weight ratioa)DVBb)
mmol g %
1 3.65 16.0 1:4 10
2 3.65 13.3 1:2 10
3 5.48 13.3 1:2 30
4 3.65 10.0 1:1 10
5 5.48 10.0 1:1 30
ht of HA and HD (core materials) to total monomers of DFHA
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Gel Permeation Chromatography (GPC)
AWaters1525/2414/717 (1525binaryHPLCpump,2414refractive-
index detector, 717 autosampler) GPC systemwas used to analyze
molecular weight and its distribution of the amphi-RAFT agent.
ThreeWaters Styragel columns HR 4, 3, 1 were used. THFwas used
as eluent with a flow rate of 1mL �min�1. Mn of the amphi-RAFT
agent relative to polystyrene was 1 728 g �mol�1, and the PDI was
1.07. Interestingly, themolecularweight fromGPC agreedwith the
the value (1 816g �mol�1) calculated from the1H NMR spectrum
using Equation (3):
nanoc
Core
and DV
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H & Co
Mn ¼ MRAFT þNMAAMMAA þNDFHAMDFHA (3)
where MRAFT, MAA, and MDFHA are the molar mass of CDPA, MAA,
and DFHA respectively.
Preparation of Shell Cross-Linked Fluorinated
Nanocapsules via Interfacial RAFT Miniemulsion
Polymerization
0.5 g (0.1786mmol) amphi-RAFT (used in all experiments listed in
Table 1) was dissolved in 25g de-ionized water with 0.07 g
(1.75mmol) NaOH. After filtration, the amphi-RAFT aqueous
solution was re-filled with de-ionized water up to 74.9 g. 0.1 g
(1.45mmol). NaNO2 as an aqueous free radical scavenger[45] was
then added to the amphi-RAFT solution. Then pH value of the
aqueous amphi-RAFT solution was adjusted to 6.46. The oil phase
the total weight of which was fixed at 20 g contained the pre-set
corresponding amounts of fluorine-monomer DFHA and cross-
linking agentdivinylbenzene (DVB),HD,HA, andAIBN (see Table 1)
were stirred magnetically for 0.5 h at 28 8C. The aqueous solution
was then mixed with the oil phase. The mixture was stirred
magnetically for0.5h forpre-emulsification. The resultedemulsion
was then subjected to sonication using the ultrasonic processor
(JOY-II) at a power output of 600W for 15min at 25 8C to obtain the
miniemulsion. 5mL de-ionized water which contained 0.2 g SDS
was post-added to the obtained miniemulsion under stirring. The
resultedminiemulsionwas then transferred to a 250mL four-neck
round bottomglass flaskwith amechanical stirrer, a rubber plug, a
reflux cooler, and a N2 bubbler. The miniemulsion polymerization
apsules.
materials HA/HD Conversionb) HA/HD
g weight ratio %
4 1 88 1
6.7 1 84 1
6.7 1:2 92 1:2
10 1:2 85 1:2
10 1:2 84 1:2
B (precursors for shell); b)Based on total monomer weight.
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H. Chen, Y. Luo
was initiated at 70 8C after having highly pure N2 bubbled for
15min. The polymerization lasted for 6h under N2 protection. The
final monomer weight conversion in this work was all over 80%.
Fabrication of Hollow Cross-Linked Fluorinated
Polymer Particles
The latex product of the miniemulsion polymerization was de-
emulsified by adding several drops of hydrochloric acid. The
polymer solid was collected by suction filtration with a large
numberofdeionizedwaterandthendried to removeresiduewater.
The collected polymer solid was re-dispersed in THF by magne-
tically stirring for 24h to replace the core material mixture of HA
andHD. Then thewhite polymer solidpowderwasprecipitatedout
by adding hexane to THF and was dried at 40 8C for 2 h under
vacuum.
pH Measurement
ThepHof theaqueousamphi-RAFTsolutionwasmonitoredbyapH
meter (LEICI PHS-2C) with an electrode E-201-C.
DSC Analysis
The glass transition temperature (Tg) of the copolymer was
measured with a Q200 differential scanning calorimeter (TA
instruments). The samplewas cooled to –60 8C at 50 8C �min�1 and
maintained for 2min, then scanned at a heating rate of
20 8C �min�1 from –60 to þ140 8C.
Fourier-Transform Infrared (FT-IR) Spectroscopy
IR spectra were measured on a Nicolet 5700 infrared spectrometer
with using DTGS KBr detector. The dried hollow cross-linked
fluorinated polymer particles cast onto KBr disk. The sample
concentration in the disks was 1wt.-%.
Gel Fraction Measurement
The fluorinated copolymer were collected from the latex by being
dried at 160 8C under vacuum for 4h to remove core materials HA
and HD. 0.6 g dried copolymer was packaged by filter paper, and
was extracted for 48h with THF as solvent in a Soxhlet extractor.
The package was then vaporized at room temperature and then
dried under vacuum at 40 8C until constant weight (W). The gel
fraction (Gc) was calculated from Equation (4):
Gc ¼0:6�W
0:6(4)
Transmission Electron Microscopy (TEM)
TEM was performed on JEM-1230 from JEOL at the operating
voltage of 80 kV. The samples were made by dipping 200-mesh
carbon-coated coppergrids into thediluted latexproducts and then
dried at room temperature for a while.
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Scanning Electron Microscopy (SEM)
The hollow fluorinated polymer particles were observed by SEM
(Hitachi S4800 and ULTRA 55, 5.0 kV).
Results and Discussion
Synthesis of Shell Cross-Linked Fluorinated PolymerNanocapsules
In the case of polystyrene nanocapsules, it has been found
that the homogeneous nucleation could lead to the
formation of the solid particles.[41] When the amphiphilic
RAFT agent was designed to be a random copolymer of
styrene and methyl methacrylate, the homogeneous
nucleation could be suppressed by lowering pH values.[41]
The same strategy was adopted here. So, the amphi-RAFT
agent was designed to be the random copolymer of MAA
andDFHA, and thepHvaluewasadjusted to6.46. To further
suppress the homogeneous nucleation, the oil-soluble
initiator AIBN was used, and NaNO2 was added to be an
aqueous radical scavenger.[45] Once the miniemulsion was
formed, a small fraction of SDS was added to prevent the
possible coagulation of the minidroplets. In our first
experiment (Exp 1, see Table 1), the core/shell weight ratio
was set to 1:4. The core materials were the mixture of half-
to-half HD and HA, of which HA was co-solvent of
monomers and HD. DVB is cross-linker, which would
covalently hold the polymer shell to be an integrity. The gel
fraction of the product polymer was measured to be 99%,
suggesting the fluorinated polymer shell was highly cross-
linked. The typical TEM image of the particle product from
the miniemulsion polymerization is presented in
Figure 2(a). From Figure 2(a), most particles have a core/
shell structure and statistic from TEM image shows that
more than 95% of total existing particles are nanocapsules
except those small solid particles whose diameters are
below 60nm. The particle sizes are from 30 to 200nm in
diameter with the statistical number-average diameter
Dn
� �114nm,number-average shell thickness dn
� �15.8 nm,
and coefficient of variation (CV) 26.9%. The shell thickness
agrees well with the theoretical shell thickness
[dn;theo ¼ 15.3 nm], calculated using Equation (5):
011, 21
H & Co
dn;theo ¼Dn
2� 1�
ffiffiffiffiffiffiffiffiffiffiffiffiffirs�rdrs�rc
3
r� �(5)
where rs is the density of the polymer shell of the
nanocapsules, rd is the density of miniemulsion droplets
before polymerization, and rc is the density of core
materials within a few monomers according to corre-
sponding conversion. The core/shell weight ratio of
the resulted nanocapsules was statistically estimated to
be 1:2.5 from TEM data, which is close to the theoretical
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Figure 2. Typical TEM images of particles from (a) the interfacial RAFT miniemulsionpolymerization; (b) the conventional miniemulsion polymerization.
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value 1:2.4 at 88% monomer conversion. From the TEM
image, some particles are deformed. From DSC, the glass
transition temperature (Tg) of the polymer shell was
estimated to be about 13 8C. Such a deformation of
particles may be understandable considering HA might
be partly vaporized during TEM measurement.
As a comparison, the conventional miniemulsion poly-
merization with 0.6 g SDS as surfactant replacing the
amphi-RAFT as surfactant was carried out. 1wt.-% MAA
based on the total monomer was used, whichwas found to
facilitate the formation of core/shell structures.[26] Actu-
ally, theMAA amount incorporated in the polymerwas the
same as the preciously interfacial RAFT miniemulsion
polymerization. The resultedparticles are irregularwithout
clear core/shell structures as evidenced in Figure 2(b).
This is expected from both thermodynamics and
kinetics aspects. In thermodynamics, poly(DFHA) is more
Figure 3. FT-IR spectrum of hollow fluorinated polymer particles(Exp 1).
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hydrophobic than the mixture of HD/HA.
According to Torza and Mason[33] and
Sundberg,[34] thenanocapsuleswithpoly-
mer shell should not be thermodynami-
cally preferred. In kinetics, it has been
shown that the cross-linked polymer
shells are often difficult to form due to
the failure of movement of cross-linked
polymer chains in a conventional (mini)-
emulsion polymerization.[28] The sharp
contrast in the particle morphology as
evidenced in Figure 2(a) and (b) clearly
suggests that the interfacial RAFT mini-
emulsion polymerization overcomes not
only the kinetic but also thermodynamic
barriers to form well-defined core-shell
structures, which are often confronted in
the conventional miniemulsion polymerization. Figure 3
shows the FT-IR spectrum of the hollow cross-linked
fluorinated polymer particles of Exp 1. The characteristic
signals of poly(DFHA) are seen from the C¼O stretching
peak at 1 760 cm�1, the peaks of 1 250 and 1 171 cm�1
associated with the motions of the –CF2– chain, and the
peak at 692 cm�1 from the combination of rocks and
wagging vibration of –CF2CF3 groups. The absorption peaks
withmoderate intensity at 1454and900 cm�1 are fromthe
aromatic ring of DVB. A broad absorption peak from –OH is
seen at 3 490 cm�1, indicating that –COOH groups derived
from the amphi-RAFT agent were still anchored on the
surface of the hollow fluorinated polymer particles.
The Influence of Core/Shell Ratios on the ParticleMorphology
The core/shell ratio of the nanocapsules was adjusted by
changing the weight ratio of monomers to core materials
from 1:4 (Exp 1), 1:2 (Exp 2) to 1:1 (Exp 4), as referred to
Table 1. In the case of Exp 1 and Exp 2,moreHA is needed to
formahomogeneous oil solution.With the core/shell ratios
increased, the core/shell structures look more deformed
under TEM as evident in Figure 4(a) and (b) [note: the
particle morphology of Exp 1 is shown in Figure 2(a)]. The
theoretical simulations have shown that the mechanical
properties could dramatically decrease when decrease in
thickness for a nanolayer of polymer.[46] To increase the
mechanical strength of the polymer shell, the cross-linker
amountwas increasedupto30wt.-% (Exp3andExp5, see in
Table 1). As seen in Figure 4(c) and (d), the core/shell
particles become much less deformed, as expected. In such
cases, for the core/shell ratio 1:2 (Exp 3), Dn ¼ 94nm,
CV¼ 31.6%, and dn ¼ 8.9 nm, which is a little thinner than
the theoretical value 9.7 nm. The average core/shell weight
ratio of the resulted nanocapsules is 1:1.3, compared to
the theoretical 1:1.5 (92% total monomers conversion). In
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Figure 4. TEM images of fluorinated polymer nanocapsules with different core/shellratios prepared via interfacial RAFT miniemulsion polymerization. (a) 1:2, 10wt.-% DVB;(b) 1:1, 10wt.-% DVB; (c) 1:2, 30wt.-%DVB; (d) 1:1, 30wt.-% DVB.
Figure 5. TEM and SEM images of hollow fluorinated polymer nanostructures. (a) TEM.(b) SEM.
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H. Chen, Y. Luo
the case of the core/shell ratio 1:1 (Exp 5), Dn ¼ 99nm,
CV¼ 24.2%, and dn ¼ 9.1 nm, thicker than theoretical value
that is 7.7 nm (84% monomer conversion). Form TEM
images, it is found that all the particles are core/shell
structures, even those small particles whose diameters are
below 40nm in Figure 4(c) and (d).
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Hollow Fluorinated PolymerStructures
The hollow fluorinated polymer struc-
tures can be made simply by removing
the liquid core materials. For an example,
the dried nanocapsules of Exp 5 were re-
dispersed in THF. Thus, the corematerials
were replaced by THF. The later THF core
could be easily vaporized at room tem-
perature under reduced pressure. No HD
melting peak was found in DSC measure-
ment of the hollow polymer particles,
indicating that the core materials were
completely removed. From the TEM pic-
tureshowninFigure5(a), thewell-defined
core/shell structures are clearly seen. The
hollow particle shows a bit coarse shell
and somewhat inhomogeneous sphere
shape, due to its shell highly crosslinked.
It is noted that THF is a good solvent for
poly(DFHA), so the polymer shells were
actually cross-linked into integrity so that
the core/shell structures were able to
resist the dissolution of THF. As a matter
of fact,most of thehollownanostructures
remained spherical though a small frac-
tion of collapsed particles were found as
shown in the SEM image of Figure 5(b).
There several hollow particles are
observed having a dimple, this may be
led by the thin shell of the hollow
particles, because a part of the shell
collapsed and left a dimple when core/
shell ratio of thenanocapsules is up to 1:1.
Conclusion
The nanocapsules with cross-linked poly-
(DFHA) shell were synthesized by the
interfacial RAFT miniemulsion polymer-
ization using the amphi-RAFT agent. The
utility of the interfacial RAFT miniemul-
sion polymerization overcame the ther-
modynamic and kinetic barriers in a
conventional miniemulsion polymeriza-
tion. The well-defined hollow fluorinated
polymer structures were obtained by the subsequent
removal of the liquid core materials. The core/shell ratio
was be easily tuned up to 1:1. In the case of high core/shell
ratio of 1:2 and 1:1, the nanocapsules were severely
deformed, which was improved by the increase of DVB
amounts up to 30wt.-%. The resulted hollow nanoparticles
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withfluorinatedpolymershellwouldbeof interest inmany
fields such as use as oxygen carriers, fuel cells, and
membranes.
Acknowledgements: This work was financially supported by theNational Science Foundation of China (NSFC) (#20836007) as wellas Program for Changjiang Scholars and Innovative ResearchTeams in University.
Received: October 22, 2010; Revised: December 8, 2010; Publishedonline: January 28, 2011; DOI: 10.1002/macp.201000664
Keywords: fluoropolymers; hollow particles; miniemulsion poly-merization; nanoparticles; reversible addition fragmentationchain transfer (RAFT)
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