first nitroxide-mediated controlled/living free radical polymerization in an ionic liquid
TRANSCRIPT
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First Nitroxide-Mediated Controlled/Living Free
Radical Polymerization in an Ionic Liquid
Julia Ryan,1 Fawaz Aldabbagh,*1 Per B. Zetterlund,*2a Bunichiro Yamada*2
1Department of Chemistry, National University of Ireland, Galway, IrelandFax: 00353 91 525700; E-mail: [email protected]
2Department of Applied and Bioapplied Chemistry, Faculty of Engineering, Osaka City University, 3-3-138 Sugimoto,Sumiyoshi-ku, Osaka 558-8585, JapanE-mail: [email protected]
Received: January 7, 2004; Revised: February 25, 2004; Accepted: March 1, 2004; DOI: 10.1002/marc.200400006
Keywords: controlled/living polymerization; ionic liquids; kinetics (polym.); nitroxides; radical polymerization
Introduction
1-Alkyl-3-methylimidazolium hexafluorophosphates are
non-volatile, room-temperature, ionic liquids. They have
been developed as air- and water-stable reaction media with
the potential to be recycled, and have been shown to accele-
rate and improve the yields of common organic reactions.[1]
The most notable are the commercially available 1-butyl-
3-methylimidazolium hexafluorophosphate [bmim][PF6]
and 1-hexyl-3-methylimidazolium hexafluorophosphate
[hmim][PF6] (Scheme 1).
Recently, the first conventional free radical polymer-
izations of methyl methacrylate (MMA) and styrene in
[bmim][PF6] were reported, and were observed to have
rates of polymerization and molecular weights approxi-
mately ten times higher than those obtained in benzene.[2]
The rate constants of propagation (kp) and termination (kt)
for the polymerization of MMA in [bmim][PF6] have been
determined by pulsed laser polymerization (PLP).[3] The
observed acceleration and higher molecular weights in
comparison to solution and bulk polymerizations were ex-
plained in terms of a combination of a larger kp and smaller
kt attributable, respectively, to the high polarity and high
viscosity of the ionic liquid.[3]
Summary: The controlled/living radical polymerizationsofmethyl acrylate in 50%v/vof an ionic liquid initiated by thealkoxyamine generated in situ from 4-oxo-2,2,6,6-tetra-methyl-1-piperidinyl-N-oxyl (4-oxo-TEMPO) and 2,20-azoi-sobutyronitrile (AIBN) at 140–155 8C are reported. Thenumber-average molecular weights increased linearly withconversion, and polydispersity indices are approximately1.4 in the best case. The rates of polymerization were greaterthan in anisole, and similar to the rate of spontaneous poly-merization in the ionic liquid.
Mn (filled symbols) andMw=Mn (open symbols) vs. conver-sion for the MA polymerization in the presence of [4-oxo-TEMPO]/[AIBN] (2.8:1) in 50% v/v anisole with 0.03 M
AIBN (squares) and 50% v/v [hmim][PF6] with 0.03 MAIBN(circles), and 0.06 M AIBN (triangles).
Macromol. Rapid Commun. 2004, 25, 930–934 DOI: 10.1002/marc.200400006 � 2004 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim
930 Communication
a Current address: Graduate School of Science and Technology,Kobe University, Kobe 657-8501, Japan;E-mail: [email protected]
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The three most well-known controlled/living free radical
polymerization techniques are nitroxide-mediated poly-
merization (NMP), atom transfer radical polymerization
(ATRP), and reversible addition-fragmentation chain trans-
fer (RAFT).[4] There are several reported controlled/living
radical polymerizations in ionic liquids by ATRP,[5–8] re-
verseATRP,[9] and RAFT.[10] For these systems, controlled/
living polymerization characterized by the formation of
narrow polydispersity polymers and significant rate en-
hancement compared to polymerizations in volatile organic
solvents (VOS) were achieved. Here we report the first
NMP in an ionic liquid, namely the polymerization of
methyl acrylate (MA) in 50% v/v [hmim][PF6]mediated by
the commercially available nitroxide, 4-oxo-2,2,6,6-tetra-
methyl-1-piperidinyl-N-oxyl (4-oxo-TEMPO). It has pre-
viously been demonstrated that acrylate polymerizations
proceed in a controlled/living manner under appropriate
experimental conditions in the presence of TEMPO.[11,12]
MA was chosen for study because of its appreciable solu-
bility in [hmim][PF6],[6] and the fact that the resultant poly-
mer could be completely precipitated out of the reaction
medium, which was successfully re-cycled.
Experimental Part
Materials
Commercially obtained MAwas freshly distilled under reduc-ed pressure prior to all polymerizations. Anisole, 2,20-azoiso-butyronitrile (AIBN), and 4-oxo-TEMPO were obtainedcommercially, and theAIBNwas recrystallized frommethanolat 0 8C prior to use. [hmim][PF6] was prepared according to aliterature procedure from 1-methylimidazole, chlorohexane,and aqueous hexafluorophosphoric acid.[13]
Polymerizations
A typical polymerization used a stock solution of 4-oxo-TEMPO (0.114 g, 0.67 mmol), AIBN (0.039 g, 0.24 mmol),and MA (4 mL, 44 mmol). A 0.5 mL quantity of the stocksolution was transferred into a glass ampoule containing either0.5 mL of [hmim][PF6] or 0.5 mL of anisole. In both cases, onagitation, a homogeneous reaction mixture resulted,[6] whichwas degassedwith several freeze-thaw cycles and sealed undervacuum. The ampoules were submerged into an aluminiumblock at 105 8C, the temperature was raised over 30 min to
the polymerization temperature and held for prescribed times.The polymerizations were stopped by cooling the solution inan ice-bath.
Conversion and Molecular Weight Measurements
Monomer conversions during polymerization in [hmim][PF6]were continuously monitored by Fourier-transform near-infrared spectroscopy (FT-NIR; Jasco INT-400 Spectrometerequipped with an MCT detector) carried out in a 5 mm o.d.Pyrex tube in a custom-made aluminium furnace. A 0.25 mLaliquot of the same stock solution was transferred into a glassampoule containing 0.25mL of [hmim][PF6], and themixtureswere degassed with several freeze-thaw cycles and sealedunder vacuum. The ampoules were held at 105 8C for 30 minin an aluminium block, and subsequently transferred to theFT-NIR furnace maintained at the polymerization tempera-ture. The consumption of MA was obtained by monitoringthe absorbance at 6 150 cm�1, which has been assigned to theovertone absorption of nC C–H. Prior to integration, the ab-sorption of [hmim][PF6] in this region was subtracted by usinga pre-recorded spectrum of poly(MA) dissolved in [hmim]-[PF6] (poly(MA) with a concentration corresponding to100% MA conversion in the polymerization sample). For theanisole experiment, a samplewas also dissolved in CDCl3, anddirectly used for monomer conversion measurements by 1HNMR spectroscopy (Jeol 400 MHz) by monitoring the vinyl-ideneMA peak at 6.1 ppm and the anisole phenyl proton peaksat 6.8 ppm as the internal standard.
Molecular weights were measured by gel permeation chro-matography (GPC)with aTosoh8000 seriesGPCsystemequipp-edwith TSK-gel columnsG5000HHR,GMultipoerHXL-M, andGMHHR-L connected in this order, using tetrahydrofuran aseluent at 40 8C. Polystyrene standards (Mn ¼ 500–1 090 000)were used for calibration.
Recycling of the Ionic Liquid
At the end of each experiment, the residual monomer wasevaporated, and the polymer precipitated with a large excess ofmethanol. The polymer was filtered off, and the filtrate wasevaporated to dryness to give a clean sample of [hmim][PF6],as confirmed by 1H NMR spectroscopy.
Results and Discussion
The initial experimentswere carried out at 155 8Cguided by
earlier work on the n-butyl acrylate/4-oxo-TEMPO system
by Listigovers et al.[11] Following their procedure, we car-
ried out MA polymerizations containing [4-oxoTEMPO]
and [AIBN] in a 2.8:1 ratio by first heating from 105 8Cto the reaction temperature of 155 8Cover 30min in order to
form in-situ polymeric alkoxyamine adducts. Consistent
with some previous NMP work on acrylates, an excess of
nitroxide was required in order to achieve reasonable con-
trol during the polymerization,[14] although the results pre-
sented here are not optimized with respect to the nitroxide
concentration. The number-average molecular weight (Mn)
Scheme 1.
First Nitroxide-Mediated Controlled/Living Free Radical Polymerization in an Ionic Liquid 931
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increased close to linearly with conversion at two different
AIBN concentrations (keeping the ratio of [4-oxoTEMPO]
to [AIBN] constant) (Figure 1). At the lower AIBN concen-
tration, there is some deviation from linearity in the higher
conversion range, probably because of irreversible termina-
tion reactions of propagating species. An increase in AIBN
concentration by a factor of two resulted in a decrease in
Mn by close to a factor two as expected for a controlled/
living system. Calculation of the theoretical Mn is not
trivial in this case since the starting point was AIBN and
free nitroxide as opposed to an alkoxyamine; it is, however,
noted that the experimental Mn’s are considerably higher
than the theoretical values as calculated based on either the
initial amounts of AIBN or free nitroxide. This is in contrast
to the polymerization carried out under identical conditions
using anisole in place of the ionic liquid with an AIBN
concentration of 0.03 M, whereMn remained close to the cal-
culated values (Figure 1). Previously reported controlled/
living polymerizations using ATRP[7] and reverse ATRP[9]
in ionic liquids also exhibited low initiation efficiencies
leading to Mn values exceeding the theoretical ones. This
was attributed to low concentration of the catalyst in the
ionic liquid (two-phase system),[7] and a ‘‘cage-effect’’ (one-
phase system),[9] respectively. Somewhat low efficiency of
a RAFT agent in an ionic liquid has also been reported,[10]
and this was speculated to be caused by poor solubility of
the RAFTagent. In our case, visual observation suggested a
homogeneous reaction mixture, but it cannot be excluded
that solubility effectsmaybe at least part of the reason for the
discrepancy between experimental and theoreticalMn’s.
The polydispersity index for the sample with the higher
AIBN concentration is 1.4 at approximately 30% conver-
sion, whereas the experiment with the lower concentration
yielded higher polydispersity indices near 1.8. The poly-
dispersity indices in the anisole experiment remained near
1.2 at low conversion, but increased significantly at higher
conversions (Figure 1). Reasonable control is thus achieved
at the higher AIBN concentration in the ionic liquid, and it
may be possible to improve the level of control by fine-
tuning the nitroxide concentration.
Polymerizations carried out in [hmim][PF6] were faster
than in anisole using the AIBN concentration of 0.03 M, as
shown in Figure 2. The rate increase is consistent with
earlier observations for conventional free radical polymer-
izations[2,3] and controlled ATRP[5] and RAFT[10] systems
in ionic liquids for the reasons outlined in the introduction.
The rate of polymerization was not significantly affected by
the AIBN concentration at a constant [4-oxoTEMPO]-to-
[AIBN] ratio. Independence of the rate of polymerization on
the alkoxyamine concentration in TEMPO-based nitroxide
mediated polymerizations of styrene[15,16] is attributable to
the propagating radical concentration being governed by
the quantity (Ri/kt)0.5 after the pseudo-steady state has been
Figure 1. Evolution of Mn (filled symbols) and Mw=Mn (opensymbols) with conversion for the polymerization of MA in thepresence of a 2.8:1 ratio of [4-oxo-TEMPO]/[AIBN] at 155 8C in50% v/v anisole with [AIBN]¼ 0.03 M (&, &), and 50% v/v[hmim][PF6] with [AIBN]¼ 0.03 M (*, *), and [AIBN]¼0.06 M (~, ~).
Figure 2. ln([M]0/[M]) vs time for the polymerization of MAat 155 8Cunder various conditions, where [M] and [M]0 denotethe instantaneous monomer concentration and the initialmonomer concentration, respectively. (A)MAonly; (B)MA in50% v/v [hmim][PF6] with [4-oxoTEMPO] and [AIBN]¼ 0;(C) and (D) MA in 50% v/v [hmim][PF6] in the presence of a2.8:1 ratio of [4-oxoTEMPO]/[AIBN] with [AIBN]¼ 0.03 M
and 0.06 M, respectively; (&) in 50%v/v anisole in the presenceof a 2.8:1 ratio of [4-oxoTEMPO]/[AIBN] with[AIBN]¼ 0.03 M. Conversions obtained by FT-NIR spectro-scopy, except for the anisole experiment which were obtainedby 1H NMR spectroscopy.
932 J. Ryan, F. Aldabbagh, P. B. Zetterlund, B. Yamada
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reached. This is because of the thermal initiation of styrene
– in analogy with this observation, our results thus suggest
that there is a source of radicals other than the thermal
dissociation of alkoxyamines. Polymerizations ofMAwere
therefore attempted in the absence of bothAIBN and 4-oxo-
TEMPO in 50% [hmim][PF6] and forMA alone. The rate of
polymerization in the ionic liquidwithoutAIBN and 4-oxo-
TEMPO (plot B) is very similar to those carried out with
AIBN/4-oxo-TEMPO (plots C and D) in analogy with the
system styrene/TEMPO in bulk (except for some differ-
ences at very low conversion to polymerizations). How-
ever, in the absence of ionic liquid (i.e., bulk MA only,
plot A), the polymerization proceeds much faster. Sponta-
neous (thermal) polymerization of acrylates at elevated
temperatures has been reported, although it is not clear if
this is because of ‘‘true’’ thermal initiation, or whether
initiation occurs by adventitious impurities.[17]
Experiments were also carried out at 140 and 130 8C in
order to investigate whether control could be achieved at
lower temperatures with the current system. TheMn vs con-
version plots exhibited close to linear behavior at both 130
and 140 8C (Figure 3). TheMn data points at 140 and 155 8Care overlapping as expected if the number of growing chains
is the same in both cases. TheMn values at 130 8C are some-
what higher, indicating a lower number of growing chains.
This may be related to a lower rate of generation of radicals
via spontaneous initiation, although the degree of control
achievedmay suggest that the number of chains originating
from thermal initiation is small relative to that derived
from the initial alkoxyamine (as is normally the case in the
NMP of styrene[16]). It could also be a result of solubility
effects being more significant at a lower temperature. The
polydispersity indices increase markedly with decreasing
temperature, giving approximately 1.8 at 140 8C and 2.1 at
130 8C. It is apparent that the degree of control deteriorateswith decreasing temperature, most likely as a result of the
rate of dissociation of the alkoxyamines not being suffi-
ciently high. Alkoxyamine thermal-dissociation rates have
been reported to increase with solvent polarity,[18,19] and it
may therefore be anticipated that the dissociation rates in
the polar ionic liquid may be higher than in bulk/or in VOS.
However, solely based on a comparison of our polymer-
ization results with 4-oxo-TEMPO in the ionic liquid,
[hmim][PF6], and anisole, it cannot be concluded whether
this is the case or not. The polymerization proceeded only
slowly at 130 8C, the conversion reaching only about 11%
in 20 h (Figure 4).
Conclusions
Controlled/living radical polymerization ofmethyl acrylate
mediated by 4-oxo-TEMPO has been successfully carried
out in an ionic liquid for the first time. The relatively high
reaction temperature of 140 8C was required to achieve
reasonable control. The number-averagemolecular weights
(Mn) increased linearly with conversion, although they
were significantly higher than the theoretical values. An
increase in the AIBN and 4-oxo-TEMPO concentrations by
a factor of two (i.e., constant [4-oxo-TEMPO]/[AIBN]) re-
sulted in a decrease inMn by close to a factor of two, but had
Figure 3. Evolution of Mn (filled symbols) and Mw/Mn (opensymbols) with conversion for the polymerization ofMA in 50%v/v [hmim][PF6] in the presence of a 2.8:1 ratio of [4-oxoTEMPO]/[AIBN] with [AIBN]¼ 0.03 M at 155 8C (*, *),140 8C (^,}), and 130 8C (&,&).
Figure 4. ln([M]0/[M]) vs time plots obtained from FT-NIRdata for the polymerization of MA in 50% v/v [hmim][PF6] inthe presence of a 2.8:1 ratio of [4-oxoTEMPO]/[AIBN] with[AIBN]¼ 0.03 M.
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no significant effect on the rate of polymerization. The latter
finding could be accounted for by showing that the poly-
merization of MA in [hmim][PF6] and bulk MA proceed in
the absence of AIBN/4-oxo-TEMPO, revealing that signi-
ficant spontaneous polymerization occurs. In contrast, a
polymerization carried out in anisole was significantly
slower than the polymerization carried out under identical
conditions in the ionic liquid, and gave molecular weights
close to the calculated values. Upon precipitation of the
polymer, the re-cycling of the ionic liquid reaction medium
was achieved.
Acknowledgement: The authors thank the Irish ResearchCouncil for Science, Engineering & Technology (IRCSET) foran EMBARK Scholarship for Julia Ryan, and Enterprise Irelandfor an International Collaboration Award.
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