Table 2. Cyclocoupling of styrene oxide and CO2 using Cu
catalystsa
Table 3. Catalyst recycling experiments using 1b for cyclo-
coupling of 2aa
O
1
b (10 mg), 10 mol % TBAB
O
Cycle
1b amt/mg
10.0
8.7
Yield/%
TON
26.0
27.4
29.1
30.5
30.1
O
Ph
a 1 mmol
CO (0.1 MPa), 28 °C, 48 h
2
O
1
2
3
4
5
74
68
54
47
42
Ph
2
3
a
6.5
Entry
Variation from the standard conditions
None
Yield/%
5.4
1
2
3
4
5
6
7
66
4.9
Without TBAB
0
aAll reactions were performed on a 1 mmol scale using 10
mol % TBAB under 2.5 MPa CO2 at 28 °C for 48 h. Yields of
isolated products are shown.
22b
Without 1b
2.85 mol % Cu(OAc)2 instead of 1b
2.85 mol % Cu(Naph)2 instead of 1b
2.85 mol % CuTPP instead of 1b
AcOEt extract was used instead of 1b
45
67
15b
25b
reaction of styrene oxide 2a was conducted using 1b under
.5 MPa CO . After the completion of the first cycle, the
2
2
a
Naph: 1-naphthoate, TPP: 5,10,15,20-tetraphenylporphinate.
reaction mixture was diluted with AcOEt and 1b was separated
by centrifugation. The recovered 1b was dried under vacuum
and reused in the next cycles. As summarized in Table 3,
Cu MOF 1b could be reused over five cycles; however, the
amounts of recovered 1b gradually decreased, and accordingly,
the yields of 3a lowered from 74% for the 1st cycle to 42% for
the fifth cycle. Nevertheless, turnover number (TON) gradu-
ally increased over reaction cycles. These results indicate that
recovered 1b maintained its catalytic activity, although the
amount of recovered 1b decreased by partial degradation with
unsticking of the 2D MOF sheets. The slight increase in TON
can be attributed to the accumulated TBAB cocatalyst. In strik-
ing contrast, copper (II) 1-naphthoate (Naph), Cu(Naph)2,
could not be recycled in a similar manner, which indicates an
advantage of the MOF catalyst regarding recyclability.
b
Yields of isolated products are shown. Crude yield determined
by H NMR analysis.
1
was carried out under 2.5 MPa CO (Entry 5). An increase in
CO pressure to 5.0 MPa did not lead to further improvement
Entry 6).
2
2
(
Several control experiments were conducted to investigate
the origin of the observed catalytic activity of 1a and 1b, as
summarized in Table 2. No reaction occurred in the absence
of TBAB, which implies that this cocatalyst is imperative
Entry 2). In contrast, TBAB alone catalyzed the cyclocoupling
to afford 3a with a low yield of 22% (Entry 3). Several
copper compounds were tested as catalysts. Because 10 mg of
(
13
1
b corresponds to 2.85 mol % Cu, 2.85 mol % of Cu(O2CR)2
was used as the catalyst. Cu(II) acetate and 1-naphthoate exhib-
ited significant catalytic activity, affording 3a in 45% and 67%
yields, respectively (Entries 4 and 5). The use of CuTPP as a
catalyst led to the formation of 3a in a lower yield than that
obtained with TBAB alone (Entry 6).14 Therefore, the catalytic
activity of the copper porphyrin was negligible, and the effect
of the carboxylate ligands on the efficiency was the same as
that observed for 1a/1b. These results suggest that the catal-
ytically active sites of 1a and 1b are the copper paddle wheel
units rather than the copper porphyrin moiety. This consid-
eration is in striking contrast to the previous study that implied
a significant contribution of the copper porphyrin moiety to the
Previous studies on epoxide-CO cyclocoupling with Cu
2
MOF catalysts have reported limitations in epoxide scope.
In general, epoxides larger than propylene oxide lowered
the product yields. Functional-group compatibility was also
neglected in those studies. We performed the reactions of vari-
ous epoxides to establish the substrate scope as summarized in
Table 4. The reaction of 2-(tert-butoxymethyl)oxirane (2b) was
conducted under the standard conditions and at atmospheric
pressure of CO furnished cyclic carbonate 3b in high yield
2
(82%), indicating that the bulky tert-butoxymethyl substituent
was tolerated by 1b (Entry 1). Acetoxymethyl derivative 3c,
propargyloxymethyl derivative 3d, and hydroxymethyl deriv-
ative 3e were also obtained in 5685% yields (Entries 24).
The oxygen functionality in the substituent was unnecessary
because both chloromethyl derivative 3f and but-3-enyl deriv-
ative 3g were obtained in 68% yields (Entries 5 and 6). Cyclic
carbonates with perfluoroalkyl substituents have been claimed
to be superior solvents for the electrolyte salt of lithium second-
ary batteries as compared to conventional ethylene and pro-
catalytic performance of MMPF-9 in epoxide-CO cyclocou-
2
pling. Moreover, the efficiency of 1a and 1b was greater than
that of HKUST-1 despite the paddle wheel units in 1a and 1b
with saturated coordination sites. Thus, the mechanism for
the activation of epoxides deserves further discussion (vide
infra). Finally, potential catalyst leaching was examined as
follows: 10 mg of 1b was stirred in AcOEt at 28 °C for 24 h,
and after centrifugation, the AcOEt supernatant was decanted
and concentrated. Subsequently, 10 mol % TBAB and 1 mmol
of 2a were added to the obtained extract, and the reaction
mixture was stirred at 28 °C for 48 h to obtain 3a in 25% NMR
yield (Entry 7). The contribution of catalyst leaching can be
neglected because the observed yield was comparable to that
of TBAB alone (Entry 2).
1
5
pylene carbonates. The perfluoroalkyl derivative 3h was
obtained in 71% yield from commercial epoxide 2h using our
method (Entry 7). Accordingly, various functional groups
including ester, alcohol, ether, terminal alkene, terminal alkyne,
chloroalkyl, and perfluoroalkyl, were well tolerated, although
unidentifiable byproducts were detected as trace impurities in
1
6
some cases. In addition, 2,2-disubstituted epoxide 2i and
cyclopentane-fused epoxide 2j could be used as substrates
(Entries 8 and 9), but the yield decreased for bicyclic carbonate
We then investigated the recyclability of the catalyst by
taking advantage of the heterogeneous nature of the MOFs. The
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