Full Papers
nents; both systems show inferior stability at this elevated
temperature, which causes side-reactions that involve the de-
protonation of the polyphenolic unit and its replacement by
2
Table 3. Catalytic coupling of 1,2-epoxyhexane and CO at 808C to afford
cyclic carbonate 4b.
[a]
[
9a,b]
NBu4.
The formation of (deprotonated) phenolate groups
causes a decrease in the ability to form extended HB networks
to stabilize catalytic intermediates, which results in higher ki-
netic barriers and thus slower reactions. Consequently, both
the nucleophile and polyphenol concentration is affected neg-
atively and the catalysis is shut down in the case of pyrogallol.
Conversely, both the catalysts based on 3d and 3i retain their
catalytic activity after prolonged use and, therefore, are more
effective systems for cyclic carbonate preparation at elevated
temperatures; compound 3d performs slightly better than 3i
in the reported time span. Importantly, a comparison of the
[
b]
Entry
Polyphenol
Amount
mol%]
NBu
[mol%]
4
I
T
[8C]
Yield 4b
[%]
[
1
2
3
4
5
6
7
8
–
0
1.6
2.5
1.6
0.8
1.6
3.2
1.6
0.8
80
80
80
80
80
80
80
80
17
>99
>99
80
93
>99
77
3d
3d
3d
3i
1b
1b
1b
0.75
0.50
0.25
0.33
2.0
1.3
0.66
55
[
23]
[24]
pK values of 1a (9.20) and 1b (9.01) shows that the pyro-
a
[
a] 1,2-Epoxyhexane 1.0 mmol, polyphenol amount normalized with re-
spect to [OH] groups, MEK 2.5 mL, p(CO )=1.0 MPa, 18 h. [b] NMR yields
based on mesitylene as internal standard, selectivity for 4b was >99%.
gallol unit is more acidic and likely to undergo deprotonation
more easily. This causes a (much) shorter lifetime of the cata-
lyst, whereas the system based on 3d shows a comparatively
longer lifetime. This results in a better potential to obtain
higher TONs at elevated reaction temperatures. Interestingly,
the preorganization of less active resorcinol units (cf., Figure 3,
2
1
a vs. 1b) in the cavitand increases their catalytic potential
significantly compared with the pyrogallol-based system,
which underlines the importance of the catalyst structure for
effective turnover.
The influence of the time frame on the performance of the
polyphenol to act as an efficient HB donor in the activation of
epoxides was investigated with 3d and 1b in the synthesis of
4
b (Table 4; scale 10 mmol of 4a). Solvent-free (neat) condi-
tions were employed to favor the kinetics, and the use of nu-
cleophile alone again showed a considerably lower yield of 4b
(
entries 1 and 2; 7 and 32%, respectively) compared with the
Figure 4. Comparative kinetics in the formation of 4b from 1,2-epoxyhexane
and CO at 808C using 1b (1.3 mol%), 3d (0.50 mol%), and 3i (0.33 mol%).
Conditions: 1,2-epoxyhexane 1.0 mmol, NBu I 1.6 mol%, 2.5 mL,
p(CO )=10 bar, 808C. Note that in all reactions the same molar amount of
phenol groups was used.
use of both 3d and NBu I in combination (entries 2 and 4; 46
4
2
4
2
Table 4. Comparison of 3d/NBu
coupling of 1,2-epoxyhexane and CO
b. n.a. stands
4
I and 1b/NBu
4
I as binary catalysts in the
2
at 808C to afford cyclic carbonate
[a]
4
for
not
applicable.
ophile were tested (entries 2–5) and a similar ratio was main-
tained between the catalyst components (ratio NBu I/[OH]
4
groupsꢀ3.3). For the catalyst based on 3d, the conditions re-
ported in entry 3 still produced a quantitative yield of 4b,
whereas a further decrease of the amount of catalyst to
[a]
[c]
[d]
[e]
[f]
Entry Catalyst
OH units
[mol%]
t
Yield of 4b
TON
TON
c
TOF
c
[mol%]
[h] [%]
0
.25 mol% 3d/0.8 mol% NBu I showed a modest decrease in
4
yield to 80% (entry 4). For comparison, we used a similar
amount of catalyst derived from 3i (cf., entries 3 and 5), and
a very high though not quantitative yield of 4b was observed.
Remarkably, under these conditions, the catalyst based on 1b
produced a markedly lower yield of 4b (77%; cf. entries 3 and
1
2
3
4
5
6
7
–
–
–
–
1
7
–
–
–
–
–
–
488
29
n.a.
19
n.a
18 32
46
3d, 0.010 0.080
3d, 0.010 0.080
3d, 0.010 0.080
1b, 0.026 0.080
1b, 0.026 0.080
1
575 488
925 525
1225
750 350
825
18 74
30 98
18 60
30 66
n.a.
n.a
7
), which shows the superior performance of the resorcin[4]-
and pyrogallol[4]arene-based catalysts at 808C.
To investigate this in more detail, the full kinetic profiles for
each of the catalyst systems reported in entries 3, 5, and 7
[a] 1,2-Epoxyhexane 10.0 mmol, polyphenol amount normalized with re-
spect to [OH] groups (see third column), neat conditions, p(CO
1.0 MPa, NBu 1.6 mol%. [b] Total amount of OH (phenol) units.
c] NMR yields based on mesitylene as internal standard, selectivity for 4b
was >99%. [d] TON=total turnover number based on molar amount of
phenol groups. [e] Corrected TON using the measured background con-
versions, see entries 1 and 2. [f] Corrected average TOF per hour using
the measured background conversions, see entries 1 and 2.
2
)
=
4
I
[
(
Table 3) were determined (Figure 4). The pyrogallol catalyst
system reaches a plateau in the conversion of around 70%
after 6 h, which barely increases thereafter. This is in line with
our previous results using either 1b or 2 as catalyst compo-
ChemSusChem 2016, 9, 749 – 755
752
ꢀ 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim