Journal of the American Chemical Society
Communication
Scheme 1. (a) Structure of the Dicyclopentene Monomers and
(b) Reaction Scheme of the Tandem RO/RCM
Polymerization and Proposed Polymerization Pathway for the
Selective Formation of Five-Membered Ring Repeat Units
Table 1. Tandem RO/RCM Polymerizations of M1−3
a
b
conc.
(M)
time
(h)
Mn
conv
a
entry monomer
M:C
(k)
PDI
(%)
1
2
3
4
5
6
7
8
9
M1
M1
M1
M2
M2
M2
M3
M3
M3
50:1
150:1
250:1
50:1
0.5
0.5
0.5
1.5
1.5
1.5
1.5
1.5
1.5
12
12
12
24
24
48
24
48
48
13.8
38.0
52.3
25.9
66.2
114.5
29.9
62.9
114.4
1.79
1.91
1.83
1.53
1.91
2.14
1.48
1.70
1.90
100
100
100
100
97
150:1
250:1
50:1
98
100
97
150:1
250:1
95
a
Determined by THF SEC calibrated using polystyrene standards.
Conversion was determined by crude H NMR analysis
b
1
The structure of purified P1 was characterized with NMR
(Figure 1, Figure S2), which clearly confirmed the formation of a
monomers having 3-substituted cyclopentene moieties would
polymerize at all. The Grubbs group reported that the ROMP of
3-substituted cyclopentene derivatives always failed,11 because
the substituent at the 3-position increased the steric hindrance
and decreased the ring strain, thereby preventing the ROMP.
The second issue was to determine how to control the competing
ROM and RCM equilibrium of the cyclopentene moieties in the
monomer so that the desired, structurally well-defined polymers
would be produced selectively (Scheme 1b). For example, if the
ROMP became dominant, a cross-linked gel was produced. Even
if the cascade RO/RCM reaction did occur, there were two
possible pathways depending on the orientation of the
approached catalyst. Only Pathway A was a productive pathway
for the tandem polymerization, because the second RCM step
was favored due to the proximity effect. On the other hand, in
Pathway B, a new carbene underwent RCM back to the
monomer (Scheme 1b). Thus, optimizing the polymerization
condition to control the competing equilibrium between ROM
and RCM was the key to the successful tandem polymerization.
Initially, to search for the most suitable catalyst, we screened
various catalysts for the tandem RO/RCM polymerization of
M1. Generally, a first-generation Grubbs catalyst (Catalyst 1)
has lower activity than that of second- or third-generation
Grubbs catalysts. In our system, however, Catalyst 1 showed the
best performance when comparing the monomer consumptions
Figure 1. 1H NMR spectrum of P1.
low ring-strained, five-membered, 2,5-dihydrofuran backbone.
Also, an internal olefin with an E:Z ratio of 5:1 for the acyclic
olefin was observed. Interestingly, M1 was polymerized at
concentrations <0.1 M despite possessing the low-strained
cyclopentene and the substitution at the 3-position. This finding
was in sharp contrast to the case of cyclopentene, which was
seemingly a more reactive monomer but did not undergo ROMP
at concentrations <0.8 M.12 Instead, at concentrations below the
critical monomer concentration for the ROMP, the cascade RO/
RCM occurred to produce the polymer with a rearranged
backbone with the 2,5-dihydrofuran moiety, implying that the
2,5-dihydrofuran backbone moiety in P1 was thermodynamically
more stable than the cyclopentene in the monomer. Also, due to
the substitutions at the 2- and 5-positions on dihydrofuran, the
reverse reaction or depolymerizion would be slower than chain
propagation.
1
via H NMR (Figure S1). Next, we screened the reaction
concentration to determine the effect on the polymerization. At
0.1 M, M1 with a monomer:catalyst ratio (M:C) of 50:1 was
successfully polymerized into poly(2,5-disubstituted-2,5-dihy-
drofuran) with 87% conversion after 24 h. To shorten the
reaction time, we increased the concentration up to 1 M, but an
insoluble cross-linked gel formed within 10 min, meaning that
the concentration reached its critical concentration at which the
ROMP of the cyclopentene moiety became dominant. This
finding was somewhat expected because the critical monomer
concentration for the ROMP of the cyclopentene is 0.8 M at 25
°C.12 On the other hand, at 0.5 M, full conversion was obtained
after 12 h without any cross-linking, and simple precipitation in
methanol produced a rubbery polymer with moderate yields.
When decreasing the catalyst loading or increasing the M:C ratio
to 150:1 and even 250:1, we achieved quantitative conversion
under optimized conditions, producing P1 with Mn of 13.8−52.3
kDa in proportion to the M:C ratio (Table 1, entries 1−3).
To broaden the monomer scope, we investigated the tandem
polymerization of M2 and M3 in which two cyclopentenes were
connected by nitrogen and carbon, respectively. Unlike M1, the
analogous polymerizations of M2 and M3 at 0.5 M did not
achieve full conversions, but qualitative tandem polymerization
without any cross-linking occurred when the concentration
increased to 1.5 M. It seems that the ring-strain and the
competing equilibrium between ROM and RCM for M2 and M3
were slightly different than those for M1. Regardless, both
monomers efficiently underwent the tandem polymerization
even with low catalyst loading with M:C ratios of 250:1, and the
Mn value of the resulting P2 and P3 were roughly controlled and
proportional to the M/C ratios (Table 1, entries 4−9), and
structures of purified P2 and P3 were also characterized by NMR
(Figures S3, S4, S9, and S10) However, in all three cases, the
polydispersity index (PDI) values were broad due to chain-
transfer reactions.
B
J. Am. Chem. Soc. XXXX, XXX, XXX−XXX