9062 Chem. Commun., 2012, 48, 9062–9064 This journal is c The Royal Society of Chemistry 2012
Cite this: Chem. Commun., 2012, 48, 9062–9064
Combining chemoenzymatic monomer transformation with
ATRP: a facile ‘‘one-pot’’ approach to functional polymersw
Changkui Fu,aLei Tao,*
aYun Zhang,
aShuxi Li
aand Yen Wei*
ab
Received 28th June 2012, Accepted 20th July 2012
DOI: 10.1039/c2cc34633h
A facile ‘‘one-pot’’ chemoenzymatic-ATRP has been successfully
developed through the combination of copper-catalytic ATRP and
enzyme-catalytic monomer transformation reactions.
‘‘One-pot’’ synthesis is a strategy to improve the chemical
reaction efficiency whereby a reactant is sequentially subjected
to reactions in just one reactor. A ‘‘one-pot’’ strategy is much
desired by chemists due to its avoiding arduous separation and
purification of the intermediates, improving chemical yield,
as well as saving time and resources. In polymer chemistry,
‘‘one-pot’’ processes have been achieved by exquisite combination
of some compatible reactions with polymerization, resulting in
the concerted and facile syntheses of elegant polymers with
pre-designed functionalities and structures.1–5 However, some
of such ‘‘one-pot’’ polymerizations are carried out under harsh
conditions (i.e. complex catalysts/reactants or high temperature),
which greatly counteracts the advantages of the ‘‘one-pot’’ system.
On the other hand, enzymes are regarded as green catalysts for
a variety of reactions. Compared with conventional synthetic
catalysts, enzymes appear to be more environmentally friendly
under milder conditions with high efficiency and high selectivity.6
Thus, combining enzymatic reactions with the polymerization
process represents an alternative promising approach for the
development of facile synthesis of sophisticated polymers.
Atom transfer radical polymerization (ATRP) is a potent
methodology to prepare well-defined polymers. Because of its
mild reaction conditions, general applicability of monomers and
controllable features, ATRP has been proven to be a powerful
tool for the synthesis of polymers with designed molecular
weight, composition, architecture as well as functionality.7–15
Previous studies have suggested that some enzymatic reactions
can co-exist with the ATRP process.16 An outstanding example is
the ‘‘one-pot’’ synthesis of copolymers in supercritical CO2 by
combining the enzymatic ring-opening polymerization (ROP) of
e-caprolactone (e-CL) with the ATRP of (meth)acrylates. The
enzyme–chem-dual catalytic system is robust under reaction
conditions and both catalysts (enzyme and copper) tolerate
each other, leading to one step synthesis of well-defined block
or graft copolymers.17–20 However, besides the combination of
enzyme mediated ROP and ATRP process, there are few reports
referred to new ‘‘one-pot’’ chemoenzymatic polymerization tandem
systems. To take full advantage of enzymes, the excellent green
catalysts, deep insight and extension of the scope of enzyme–
chem-dual catalytic polymerization are still in need to develop
efficient and versatile synthetic strategies to functional
polymers.
Herein, we demonstrate a novel ‘‘one-pot’’ polymerization
strategy by combination of lipase-catalytic monomer transforma-
tion and copper-mediated ATRP to prepare polymers with
designed molecular weight, composition, and transformed side
groups. This facile ‘‘one-pot’’ synthetic strategy involves an in situ
enzymatic transesterification accompanying with the living
radical polymerization process. The synthetic strategy we have
applied is summarized in Scheme 1.
Commercially available Novozym 435, Candida antarctica
lipase B (CALB), was used to catalyze the transesterification
between fluoridated monomer 2,2,2-trifluoethyl methacrylate
(TFEMA) and alcohols (ROH) to generate the target monomer
R methylacrylate (RMA). The new formed RMA participates in
the ATRP process sequentially as a comonomer with TFEMA,
i.e., the initiator ethyl 2-bromoisobutyrate (EBiB) induces the
copolymerization of TFEMA and the gradually generated
RMA, resulting in copolymers with transformed –R side groups.
The excellent tolerance of many functional groups and the
controllable polymerization process of ATRP allow for the
Scheme 1 ‘‘One-pot’’ chemoenzymatic-ATRP for polymer synthesis
via in situ enzymatic monomer transformation.
aDepartment of Chemistry, Tsinghua University, Beijing 100084,P. R. China. E-mail: [email protected];Tel: +86-010-62792604
bKey Lab of Organic Optoelectronic & Molecular Engineering ofMinistry of Education, Department of Chemistry,Tsinghua University, Beijing 100084, P. R. China.E-mail: [email protected]
w Electronic supplementary information (ESI) available: Detailedexperimental description and results including 1H NMR spectra,GPC results etc. See DOI: 10.1039/c2cc34633h
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coherent cooperation of the enzyme catalytic system. To achieve
the ‘‘one-pot’’ chemoenzymatic-ATRP process, the transesterifica-
tion rate should match well with that of chain propagation of
polymerization. Ideally, considerable new monomer RMA should
be quickly generated and participate in the ATRP process together
with the acyl donor monomer. Thus, TFEMA is chosen as the
acyl donor monomer for the in situ monomer transformation due
to its much higher reactivity for enzymatic transesterification with
alcohols than other (meth)acrylates such as methyl methacrylate
(data not shown). Typically, the chemoenzymatic-ATRP of
TFEMA in the presence of hexanol was selected as an example
in the next detailed elucidation. The polymerization was
carried out at 45 1C using CuBr–4,40-dinonyl-2,20-dipyridyl
(dNbpy) as catalyst–ligand for ATRP. Since 2,2,2-trifluoro-
ethanol, the by-product from the transesterification of TFEMA
with alcohols, was found to hinder greatly the ATRP process
(data not shown), an equivalent amount of triethylamine (TEA)
was added into the reaction system to ensure the smooth
polymerization. Kinetics studies of the reaction revealed that
two stages exist during the ‘‘one-pot’’ chemoenzyamtic-ATRP
process (Fig. 1a). In the first stage (initial three hours), the
enzymatic transformation of TFEMA to hexyl methacrylate
(HMA) quickly proceeded, resulting in almost no TFEMA left
in the polymerization system after 3 h (Fig. S1b, ESIw).Meanwhile, 29% of total monomers polymerized to form
the poly(TFEMA)-co-poly(HMA) copolymer (Fig. 1a), which
contained approximately 78% of poly(HMA) proportion in
the copolymer composition (Fig. S2 and S3, ESIw).After the first stage, the monomers remaining in the system
were almost entirely HMA (Fig. S1b, ESIw). Thus, the secondstage could be regarded as the controlled homopolymerization
of HMA, and the polymerization continuously proceeded to
high monomer conversion (24 h, B84%, Fig. 1a). The ATRP of
HMA exhibited linear pseudo-first-order kinetic plots (Fig. 1a), the
molecular weights increased linearly with monomer conversions
and all the polymers had narrow molecular weight distributions
(PDI B 1.35) (Fig. 1b and 2a), indicative of a well-controlled
ATRP process in the presence of enzyme.
The 1H NMR spectrum of the final obtained polymer is
shown in Fig. 2b. The peaks corresponding to the ester groups
of poly(TFEMA) and poly(HMA) appeared at 4.30 ppm and
3.90 ppm, respectively. According to the integral ratio of the
peaks at 4.30 ppm and 3.90 ppm, the fraction of poly(HMA)
contained in the obtained polymer was calculated to be
approximately 90%, suggesting that the final obtained polymer
is akin to a poly(HMA) homopolymer with a short domain of
gradient poly(TFEMA)-co-poly(HMA) copolymer as the head
(Fig. 2b and Fig. S3, ESIw).Immobilized enzyme can be facilely isolated for reuse after
reactions. Moreover, immobilized CALB is highly stable and
can be operated at elevated temperature for thousands of hours
without significant loss in activity.21 In current work, the retained
enzyme activity after polymerization was analyzed through
enzymatic transesterification of 4-nitrophenyl acetate (4-NPA)
with methanol.22 As shown in Table 1 (No. 1), the enzyme
catalyst maintained nearly complete activity (93%) compared
with the pristine enzyme, further suggesting the excellent
compatibility of the enzymatic reaction with ATRP. The easy
separation and excellent enzyme activity maintenance after
the ATRP process provide additional advantage to the chemo-
enzymatic-ATRP system for future large scale manufacture.
Furthermore, versatility of the chemoenzymatic-ATRP system
was also examined using various alcohols as substrates (Table 1).
For primary alcohols such as hexanol, ethanol (EtOH), benzyl
alcohol (BzOH) and poly (ethylene glycol) methyl ether (mPEG350),
the transesterification of TFEMA cooperated well with ATRP
while the enzyme retained excellent activity (Table 1, No.1–4), The1H NMR analyses of the obtained polymers indicated that the
principal polymer compositions (B75–90%) are the poly(RMA)
(Fig. 3). Moreover, all obtained polymers have predesigned mole-
cular weights and narrow PDIs (B1.40), indicating well-controlled
ATRP processes.
Using secondary alcohols such as iso-propanol (iPA) in the
chemoenzymatic-ATRP system, approximately 56% of TFEMA
Fig. 1 ‘‘One-pot’’ chemoenzymatic-ATRP containing in situ transfor-
mation from TFEMA to HMA: (a) transesterification conversion,
monomer conversion and the kinetic curve versus polymerization time;
(b) molecular weight and PDI of the polymer versus monomer conver-
sion. Novozym 435= 0.50 g; [EBiB] = 12.5 mM; [dNbpy] = 18.75 mM;
[CuBr] = 6.25 mM; [TFEMA]0 = 1.0M; [Hexanol]0 = 1.0 M; [TEA] =
1.0 M in 6.0 mL of toluene at 45 1C.
Fig. 2 (a) GPC curves of polymers during the polymerization;
(b) 1H NMR spectrum (CDCl3) of poly(TFEMA)-co-poly(HMA)
after purification.
Table 1 ‘‘One-pot’’ chemoenzymatic-ATRP of TFEMA andalcoholsa
No. AlcoholConv.b
(%)RMAc
(%) Mnd PDIe
Retained enzymeactivityf (%)
1 Hexanol 84 90 160 00 1.35 93 � 32 BzOH 44 86 9000 1.40 83 � 53 EtOH 73 75 8000 1.41 70 � 04 mPEG350 56 80 6000 1.26 80 � 45 iPA 31 61 6200 1.73 92 � 26 tBA 29 0 3900 1.50 100 � 0
a Novozym 435 = 0.50 g; [EBiB] = 12.5 mM; [dNbpy] = 18.75 mM;
[CuBr] = 6.25 mM; [TFEMA]0 = 1.0 M; [ROH]0 = 1.0 M; [TEA] =
1.0 M in 6.0 mL of toluene at 45 1C. b Calculated by 1H NMR.c The proportion of RMA in the polymer calculated by 1H NMR.d Determined byGPC. e Determined byGPC. f Determined by enzymatic
hydrolytic activity of 4-NPA.
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9064 Chem. Commun., 2012, 48, 9062–9064 This journal is c The Royal Society of Chemistry 2012
was converted into iso-propyl methacrylate (iPMA) within
initial 3 h and there was still 15% of TFEMA remaining in the
polymerization system after 5 h (Fig. S4a, ESIw), indicating a
comparatively slow enzymatic monomer transformation rate,
which is likely due to the steric hindrance of the iso-propyl
group.23 The enzyme also retained B92% activity after poly-
merization (Table 1, No. 5). However, the ATRP system
seemingly lost controllable character. The total polymerized
monomer wasB31% after 24 h, and the obtained polymer has
broad PDI (B1.73) with 61% of poly(iPMA) content in the
resulted poly(TFEMA)-co-poly(iPMA) copolymer (Fig. S4b,
ESIw). This phenomenon is probably attributed to the slow
generation of iPMA and the intrinsic low reactivity of iPMA
in such a quite low temperature ATRP system.
When tertiary alcohols such as tert-butanol (tBA) was used
as the substrate, the transesterification scarcely occurred despite
the enzyme retaining 100% activity during the polymerization
(Table 1, No. 6), the purified polymer was a homopolymer of
poly(TFEMA) with PDI B1.50 (Table 1, No. 6, Fig. S5, ESIw),corroborating the fact that tertiary alcohols are poor substrates
for CALB.24–27
In conclusion, a novel ‘‘one-pot’’ chemoenzymatic-ATRP
has been successfully developed by the combination of lipase-
catalytic transesterification and copper mediated ATRP. This
new synthetic strategy involved the tandem copolymerization
of the original monomer TFEMAwith enzymatically transformed
RMA. The enzyme CALB demonstrated selectivity to different
alcohol substrates. When primary alcohols were used, the enzyme
cooperated well with ATRP, appeared to be efficient under
ATRP conditions, and maintained nearly complete activity
after polymerization. The in situ monomer transformation
allowed us to obtain copolymers possessing different trans-
formed –R side groups depending on the substrate alcohols.
Considering the facile and versatile features, this ‘‘one-pot’’
chemoenzymatic-ATRP system could provide a general meth-
odology for sophisticated polymer synthesis and might have
potential applications in various areas such as biological and
material sciences.
This research was supported by the National Science Foun-
dation of China (21104039, 21134004) and the National 973
Project (no. 2011CB935700).
Notes and references
1 C. Cheng, E. Khoshdel and K. L. Wooley, Nano Lett., 2006,6, 1741.
2 J. Geng, J. Lindqvist, G. Mantovani and D.M. Haddleton, Angew.Chem., Int. Ed., 2008, 47, 4180.
3 D. Mecerreyes, G. Moineau, P. Dubois, R. Jerome, J. L. Hedrick,C. J. Hawker, E. E. Malmstrom and M. Trollsas, Angew. Chem.,Int. Ed., 1998, 37, 1274.
4 K. Nakatani, Y. Ogura, Y. Koda, T. Terashima andM. Sawamoto, J. Am. Chem. Soc., 2012, 134, 4373.
5 K. Nakatani, T. Terashima and M. Sawamoto, J. Am. Chem. Soc.,2009, 131, 13600.
6 A. Schmid, J. S. Dordick, B. Hauer, A. Kiener, M. Wubbolts andB. Witholt, Nature, 2001, 409, 258.
7 N. Ayres, Polym. Rev., 2011, 51, 138.8 V. Coessens, T. Pintauer and K. Matyjaszewski, Prog. Polym. Sci.,2001, 26, 337.
9 M. Kamigaito, T. Ando and M. Sawamoto, Chem. Rev., 2001,101, 3689.
10 K. Matyjaszewski and J. H. Xia, Chem. Rev., 2001, 101, 2921.11 M. Ouchi, T. Terashima and M. Sawamoto, Chem. Rev., 2009,
109, 4963.12 B. M. Rosen and V. Percec, Chem. Rev., 2009, 109, 5069.13 D. J. Siegwart, J. K. Oh and K. Matyjaszewski, Prog. Polym. Sci.,
2012, 37, 18.14 N. V. Tsarevsky and K. Matyjaszewski, Chem. Rev., 2007, 107, 2270.15 J. S. Wang and K. Matyjaszewski, J. Am. Chem. Soc., 1995,
117, 5614.16 S. J. Sigg, F. Seidi, K. Renggli, T. B. Silva, G. Kali and N. Bruns,
Macromol. Rapid Commun., 2011, 32, 1710.17 C. J. Duxbury, W. X. Wang, M. de Geus, A. Heise and
S. M. Howdle, J. Am. Chem. Soc., 2005, 127, 2384.18 S. Villarroya, K. J. Thurecht, A. Heise and S. M. Howdle, Chem.
Commun., 2007, 3805.19 S. Villarroya, J. X. Zhou, K. J. Thurecht and S. M. Howdle,
Macromolecules, 2006, 39, 9080.20 J. X. Zhou, S. Villarroya, W. X. Wang, M. F. Wyatt,
C. J. Duxbury, K. J. Thurecht and S. M. Howdle,Macromolecules,2006, 39, 5352.
21 O. Kirk and M. W. Christensen, Org. Process Res. Dev., 2002,6, 446.
22 N. Miletic, V. Abetz, K. Ebert and K. Loos, Macromol. RapidCommun., 2010, 31, 71.
23 J. F. Cramer, M. S. Dueholm, S. B. Nielsen, D. S. Pedersen,R. Wimmer and L. H. Pedersen, Enzyme Microb. Technol., 2007,41, 346.
24 E. M. Anderson, M. Karin and O. Kirk, Biocatal. Biotransform.,1998, 16, 181.
25 U. T. Bornscheuer and R. J. Kazlauskas, Hydrolases in OrganicSynthesis: Regio- and Stereoselective Biotransformations, 2nd edn,2006.
26 E. Henke, J. Pleiss and U. T. Bornscheuer, Angew. Chem., Int. Ed.,2002, 41, 3211.
27 S. Lutz, Tetrahedron: Asymmetry, 2004, 15, 2743.
Fig. 3 The 1H NMR spectra of polymers through the ‘‘one-pot’’
chemoenzymatic-ATRP of TFEMA and primary alcohols: ethanol
(a), benzyl alcohol (b) and mPEG350 (c).
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