ring-opening metathesis polymerization using polyisobutylene supported grubbs second-generation...
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Abu Bakar, K. elsaid, D. Bergbreiter and H. Bazzi, RSC Adv., 2014, DOI: 10.1039/C4RA08046G.
Soluble polymer bound second generation Grubbs Ru complex for ROMP that combines solution phase
chemistry and ease of separating the Ru
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This journal is © The Royal Society of Chemistry 2013 J. Name., 2013, 00, 1-3 | 1
Cite this: DOI: 10.1039/x0xx00000x
Received 00th January 2012,
Accepted 00th January 2012
DOI: 10.1039/x0xx00000x
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Ring-Opening Metathesis Polymerization using
Polyisobutylene Supported Grubbs Second-
Generation Catalyst
Mohammed Al-Hashimi,*a M. D Abu Bakar,a Khaled Elsaid,b David E. Bergbreiter,c Hassan S. Bazzi,*a
Olefin metathesis is among the most powerful tool for the formation of regio - and steroselective
carbon-carbon double bonds. Appling the principles of Green Chemistry to the syntheses of
polymers, by developing useful strategies to facilitate catalyst and polymer product separation
after a polymerization is vital. In the present study, phase select ively soluble polymer bound
second generation Grubbs catalyst was successfully used to carry out ring-opening metathesis
polymerization (ROMP) on norbornene and a variety of different exo-norbornene derivatives.
Polymers with low ruthenium contamination levels were achieved in comparison to the non-
supported Grubbs catalyst which required multiple precipitations. Furthermore, the bound
catalyst exhibits similar catalytic activity to its homogenous counterpart.
Introduction
The development of well-defined and highly active ruthenium
metathesis catalysts having excellent functional group tolerance
has been fundamental to the widespread application of olefin
metathesis,1-4 in particular for the synthesis of natural products
and small molecules.5
Ring-opening metathesis polymerization (ROMP) has become
an extremely valuable tool for the preparation of functional
homopolymers 6 providing a wide range of polymers with unique
architectures.7 Grubbs (G1, G2 and G3) and Hoveyda–Grubbs
(HG1 and HG2) ruthenium based catalysts are among the widely
used complexes in both academia and industry (Figure 1).8-10
Despite these advances a relatively high price of these catalysts
and the removal of Ru from the reaction product predominantly
in the pharmaceutical industry represent an important
disadvantage for their practical application. 11
Figure 1 Ruthenium-based olefin metathesis catalysts
a Department of Chemistry, Texas A&M University at Qatar, P.O. Box
23874, Doha, Qatar. *Email: [email protected]; [email protected] b Department of Chemical Engineering, Texas A&M University at Qatar,
P.O. Box 23874, Doha, Qatar. c Department of Chemistry, Texas A&M University, P.O. Box 30012,
College Station, Texas 77842-3012.†Electronic Supplementary
Information (ESI) available: Detailed experimental procedures, ICP-MS Digestion Procedure, NMR characterization, and assignment of polymers.
See DOI: 10.1039/b000000x/
The development of supported Ru catalysts for olefin metathesis
has attracted increasing interest, both from the view of
environmental (removal of heavy metal impurities) and
economic benefit (high ruthenium cost). We 12-14 and several
research groups 15-26 have reported the use of polymeric and solid
supports for immobilizing ruthenium based catalysts. Among the
several approaches the majority of articles report on using
supported Grubbs second generation catalysts G2 for ring
closing metathesis (RCM). Barrett et al. were the first to report
the immobilization of G2 on vinyl modified poly(styrene) beads,
the so called “boomerang” polymer supported catalyst was used
up to three times in RCM almost without loss of any activity.27
Blechert et al. reported the synthesis of supported G2 on
poly(styrene) Merrifield resin, the catalyst was used in RCM,
cross and enyne metathesis affording near quantitative
conversions.15 Fürstner et al. prepared hydroxyalkyl-
functionalized G2 complex and was shown to catalyze a serious
of RCM. The catalyst was recycled up to three times, but it
showed lower catalytic activity than its homogenous
counterpart.28 Weck et al. utilized poly(norbornene) as a support
for Grubbs second generation catalyst. The reactivity of the
supported NHC ruthenium complex were studied for RCM, the
authors reported good conversions yielding Ru free products. 29
Buchmeiser’s group are among the few that have reported the
use of supported G2 catalyst for ROMP. They used a monolithic
support to immobilize G2 complex, the catalyst was easily
removed by filtration at the end of the reaction. Reasonable
yields and high activity were obtained in both RCM and ROMP,
while the ruthenium residue in the products for RCM was found
to be 70 ppm.16 Grubbs et al. published the use of polyethylene
glycol (PEG) supported G2 complex. The water soluble catalyst
efficiently carried out the ROMP of norbornene derivatives,
however, low turnover numbers (TONs) for RCM was reported.
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After phase separation
In order to expand the scope of our work using soluble supports
we now wish to report the synthesis of polyisobutylene
supported Grubbs second-generation catalyst and its application
in Ring-Opening Metathesis Polymerization.
Results and discussions
Synthesis of soluble PIB-supported 2nd generation Ru
complex 6 and Characterization
Recently, we elaborated a simple synthetic protocol for
preparation of polyisobutylene (PIB)-supported N-heterocyclic
carbene (NHC) ligand 5.12 Using this methodology we
synthesized the new soluble PIB-supported 2nd generation Ru
complex 6. The synthetic routes to complex 6 are outlined in
Scheme 1. Accordingly, to a solution of N-heterocyclic carbene
ligand 5 in THF at room temperature was added potassium tert-
butoxide, resulting in the deportation of the corresponding NHC
salt to form the free carbene. In situ the free carbene was reacted
with Cl2Ru(CHPh)(PCy3)2 G1 in toluene at room temperature
and the reaction was heated to 80 °C. After purification a waxy
brown-pink oil in 60% yield was obtained.
Scheme 1 Synthesis of PIB-supported second-generation Grubbs
complex 6.
The structure of complex 6 was verified by 1H NMR, 31P NMR
and 13C NMR spectroscopy (Figure 2). As one might expect, the 1H NMR spectrum of complex 6 (Figure 2a) shows a shift for the
benzylidene proton peak from δ = 20.02 ppm (shift for the first-
generation Grubbs G1 complex) to δ = 19.05 ppm, consistent
with the parent none supported 2nd generation Grubbs complex
G2. However, at first 31P NMR spectroscopy indicated that some
triphenyl phosphine oxide was still present 31P δ = 50.04 ppm.
Using the heptane-phase selective solubility of complex 6 due to
the polyisobutylene-containing ligand to our advantage a
liquid/liquid separations using heptane/methanol was introduce
which ultimately resulted in removal of the phosphine oxide
affording the pure complex as depicted in Figure 2b.
a) 1H NMR spectrum of complex 6
b) 31P NMR spectrum of complex 6
Figure 2 NMR spectra (1H and 31P NMR) of PIB supported
complex 6.
The reaction was first evaluated using kinetic studies at room
temperature in deuterated THF (0.5 mL) using 1 mol% catalyst.
Conveniently the polymerizations were conducted in NMR tubes
at a spinning rate of 20 Hz. The conversion of monomer M7 to
polymer P8 was monitored using 1H NMR spectroscopy (Figure
3a-b). Interestingly, a marked difference in reactivity profiles is
observed for complex 6 and G2. The NB M7 was 93% converted
to polynorbornene P8 using complex 6 in 60 min resulting in a
colorless solution of polynorbornene P8 with low viscosity. In
comparison to the ROMP of NB with the parent Grubbs complex
G2, complex 6 exhibited a faster ROMP initiation with greater
than ca. 70% conversion occurring at 25 0C within the first 10
min (Figure 3c) and progressed to ca.90% in 30 min. Whereas
initiation was significantly slower with the non-supported
Grubbs complex G2 ca.31% conversion was achieved after
10min and ca.76% after 30 min. However, 99% conversion was
achieved within a 60 min. Both complexes G2 and 6 achieved
the same conversion in the 46 min 92%. Increasing the catalyst
loading of complex 6 to 1.5 mol% results in 99% conversion
after 20 min. The results for the kinetic studies obtained using
complex G2 agree well with previous published data in the
literature.30
Before phase separation
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a) 1H NMR spectra for non- b) 1H NMR spectra PIB- supported
complex G2 supported complex 6
c) Percentage conversion vs reaction time.
Figure 3 Rates of conversion of NB monomer to
polynorbornene- complexes G2 and 6.
The trans/cis double bond ratio in the polymer chain was
determined from 1H NMR spectroscopy as depicted in Figure 4.
The olefinic peaks of the monomer at δ = 5.85 ppm are replaced
by new signals at δ = 5.26 and 5.09 ppm, which correspond to
the cis and trans double bonds of the polymer, respectively. In
accord with previous reports, both complexes resulted in
polymer P8 having a slight excess of trans ratio (trans:cis ∼ 59:
41 complex G2, 51:49 complex 6).31
a) PIB supported complex 6 b) non-supported complex G2
Figure 4 1H NMR spectra in THF-d8 of trans/cis double bond
of polymer P8 using supported and non-supported Ru complex.
A slight difference in the trans/cis double bond ratio was found
between the polymers prepared using the PIB supported Ru
complex and non-supported complex (Table 1). The ratio of the
trans double bond in polymer P8 prepared with the supported
complex was lower. This small difference in stereoselectivity
corresponds to a ca. 0.17 kcal/mol difference in activation energy
for the stereoselectivity in trans/cis isomer formation for catalyst
G2 versus 6. Accounting for such small differences is
necessarily speculative. One possibility is that there is some sort
of steric effect of the PIB group. However, other studies by our
group have shown that terminally functionalized polymer
supports have no significant steric effect.32-35
Moreover, prior work did not show any significant difference in
trans/cis isomer ratio for polymerizations of a functionalized
norbornene using a low molecular weight or a PIB-bound
Grubbs-Hoveyda ROMP catalyst.12 We speculate that the PIB
groups that are associated with the active Ru alkylidene chain
growth site may produce a local solvent effect wherein they
interact with this relatively hydrophobic polynorbornene chain.
Even a modest such effect could easily account for the observed
small change in stereoselectivity for the non-supported complex
G2 versus the PIB-supported complex 6.
The reaction mixture containing the polymer and Ru catalyst
residue in THF was concentrated in vacuo then the Ru residue
was separated by dissolving the crude mixture in minimum
amount of DCM and precipitating the mixture in hexane. Thus,
the homoploymer was isolated as a white solid, while the PIB-
Ru complex remains in the hexane layer. The results obtained by
GPC analysis show that the number average molecular weight
(Mn) of 488,900 g/mol with a monomodal polydispersity index
(PDI) of 2.79, while using the non-supported Ru resulted in a
polymer having an Mn of 456,400 g/mol and PDI 2.85 as depicted
in Table 1.
Encouraged by the promising result and to examine the scope of
complex 6 we decided to investigate the performance of the new
complex on a wider range of substrates. Substituted exo-
norbornene imides were selected as the monomers due to their
ability to undergo living ROMP, as well as their ability to be
easily functionalized. We therefore prepared a variety of
monomers from Exo-oxabicyclo-[2.2.1] hept-5-ene-2,3-
dicarboximide M9. Monomers M11–M14 were synthesized
according to our previously reported method12 Mitsunobu
coupling of imide M9 with methoxy-terminated poly(ethylene
glycol) (average Mw = 2000) afforded monomer M10 (scheme
2). Monomers M17-M21 illustrated in Scheme 2 were prepared
according to the reported procedure with slight modifications.36
Reaction of exo-anhydride M16 with the appropriate
diamine(butane-1,4-diamine) or amino alcohol, 6-amino-1-
hexanol and 3-amino-1-propanol afforded monomer M17, M18
and M19 in 50-60% yield. Oxidation of the primary alcohol
M19 with CrO3 afforded the carboxylic acid derivative M20,
respectively. Coupling of monomer M20 with N-
hydroxysuccinimide (NHS) in the presence of 1-ethyl-3-(3-
(dimethylamino)propyl)carbodiimide (EDC) afforded the ester
M21.
0
20
40
60
80
100
0 5 10 15 20 25 30 35 40 45 50 55 60
% C
on
vers
ion
Time (Min)
Grubbs 2nd Gen. PIB Grubbs 2nd Gen.
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Scheme 2 Synthetic pathway for the synthesis of ROMP Monomers.
Table 1 Results for the Ru contamination and ROMP catalyzed by complex G2 and supported complex 6.
Entrya Polymers Product Yield
c (%) M
n
d (g/mol) PDI
d trans:cis Ru content
(%) ppm
1 P8 80 488,900 2.79 51:49 3.45 464
2 P8b 81 456,400 2.85 59:41 46.4 6134
3 P11 78 345,900 1.71 52:48 2.09 130
4 P12 63 821,600 1.83 46:54 0.98 71
5 P13 60 170,0000 1.11 44:56 1.82 139
6 P13b 71 125,500 2.34 46:54 16.6 1083
7 P14 80 737,600 2.0 43:57 3.41 156
8 P15 74 163,800 2.16 44:56 6.1 252
9 P17 65 Insoluble - - 9.25 543
10 P19 60 Insoluble - - 4.8 361
a 1 mol% catalyst; b Using non-supported Grubbs 2nd Generation complex G2; c Isolated yield; d Molecular weight and PDI were
determined by GPC; e Measurements were done using ICP-MS analysis, the mol % Ru is the % leached into the polymer.
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The reactivity of the PIB supported complex 6 with the
appropriate ROMP substrates M10 to M20 was evaluated
(Scheme 3). The reactions were carried out using 1 mol %
complex 6 under rigorously inert conditions in dry THF at room
temperature. The rate of monomer conversion was monitored
using 1H NMR spectroscopy recorded in CDCl3. Monomers
M11 to M15 were fully converted to the desired polymers P11-
P15 within 1 h, wherein resonances at δ 6.53 ppm for the
cyclic olefin were not observed. Interestingly, complex 6
exhibits very low activity for the ROMP of M10, M18 and M20,
showing just 7% conversion after 1.5 h at 25 °C in THF. Even
after the reaction time was extended to 24 h this showed no
particular change in the conversion. We infer the low monomer
conversion due to the decomposition of the Ru complex, yielding
the phosphonium oxide as the sole 31P product as analyzed by
NMR spectroscopy. Furthermore, interestingly, M17 and M19
resulted in formation of a white solid precipitate within minutes.
This was found to be essentially insoluble in common organic
solvents, Moreover, the analysis of the polymers by NMR
spectroscopy and GPC was made very difficult.
Scheme 3 Synthesis of homo-polymers via ROMP.
Homopolymers P11-15 were separated from the Ru residue as
described previously. GPC analysis of polymers P11-15 showed
broad PDI’s 1.2 to 1.9, which is relatively broader in comparison
to polymers synthesized by living polymerization using other
Grubbs initiators. Previously it has been shown that G2 complex
affords polymers with broad polydispersities and high molecular
weights, this can be attributed to the basicity of the tricyclohexyl
phosphine ligand.30, 37 and high catalyst loading.
Inductively coupled plasma mass spectrometry (ICP-MS)
analysis was used to determine the content of Ru leaching in the
polymer products (Table 1) by dissolving the polymers in
concentrated HNO3. As expected the Ru leaching levels are
substantially lower when using the supported complex 6 ranging
from 0.98% to 3.45%, in comparison to the non-supported
complex G2 which had a higher Ru contamination of 16.6% to
46.6% (entries 1 to 8) even after multiple precipitations with
hexane. The results compare favorably well with other systems
for the removal of ruthenium residues.
Conclusions
In summary, we have synthesized a soluble polymer bound
second generation Grubbs Ru complex for ROMP. The
supported catalyst can be easily obtained from commercially
available starting materials. The catalytic activity of the
supported complex is comparable to those of its homogenous
counterpart. In addition the supported catalyst combines solution
phase chemistry with the ease of separating the Ru form the final
product. Importantly, the ruthenium contamination in the
product was very low without the need for further purification in
comparison to the parent Grubbs catalyst that required multiple
precipitations. Currently further investigations in various types
of metathesis reactions using the supported Grubbs catalyst is
underway.
Acknowledgements
The authors gratefully acknowledge support of this work from
the Qatar National Research Fund project number: NPRP 4-
081-1-016.
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