Asymmetric Michael Reactions
COMMUNICATION
with the aminocatalyst used in the reactions involving this
species. Hence, we thought of exploiting the site isolation
principle.[13] To the best of our knowledge, the only example
of site isolation involving asymmetric organocatalytic pro-
To validate our hypothesis, a test reaction between para-
AHCTUNGTRENNUNG
ACHTUNGTRENNUNGcesses has been described by Frꢄchet et al. and involved the
use of functionalized soluble star polymers to carry out cas-
cade reactions.[14] In our case, we postulated that the use of
solid-supported catalysts might be the solution to segregate
each individual process (i.e. acetaldehyde generation and
aminocatalytic reaction), thus preventing the two catalysts
from deactivating each other. Specifically, it was envisaged
that employing a polystyrene-supported diarylprolinol cata-
lyst 1[15] in combination with the commercially available sul-
fonic acid resin 2, could preclude the deleterious acid/base
reaction (Scheme 2 and Table 2).
Solvent screeening showed that lower conversion was ach-
ieved in either dioxane, THF or MeCN, albeit the Michael
adduct 4a was obtained in the same 90% ee as in CH2Cl2
(Table 2, entries 4–6). Gratifyingly, when catalyst 2 was con-
fined in a teabag, conversion was further increased, which
we attributed to a better isolation of the catalytically active
species (compare entries 2 and 10). No product was detected
when the reaction was carried out without the supported
sulfonic acid 2 (entry 1), proving the role of paraldehyde as
a precursor for the slow generation of acetaldehyde in the
reaction media. Screening of the acid co-catalyst loading
(entries 7–11) showed that a 10 mol% of 2 (entry 10) was
optimal for conversion and enantioselectivity, although even
a 0.5 mol% of the acid catalyst (entry 8) still gave good con-
version and enantioselectivity levels. A further increase in
the amount of the acid catalyst 2 from the optimal 10 to
20 mol% caused an apparent slight decrease of conversion,
probably due to partial decomposition of 4a. Increasing the
Scheme 2. a) Catalyst incompatibility (deactivation by acid/base reaction)
and b) resorting to site isolation to circumvent the problem (induced by
supporting the incompatible catalysts onto polystyrene). TIPS=triisopro-
pylsilyl.
Table 2. Optimization of conditions for the Michael addition.[a]
loading of the polymer-supported organocatalyst
1 to
20 mol%, however, raised the conversion to 69%
(entry 12). It is noteworthy that paraldehyde was used as re-
ceived in the course of this study.
It is generally accepted that organocatalytic procedures
are tolerant to moisture and can be performed in open air.
Nevertheless, conversion was significantly increased to 91%
when the reaction was carried out in degassed anhydrous
CH2Cl2 in a glovebox (Table 2, entry 13), which indicated
that oxygen and moisture are important issues in this partic-
ular reaction.[16] To fully understand this effect, two parallel
reactions were performed. Ten equivalents of water were
added to the first reaction (entry 14), whereas oxygen was
bubbled for 10 min in the other reaction at the start
(entry 15). Despite the fact that the enantioselectivities
matched the result previously obtained in the glovebox, con-
version sharply decreased in these two tests. Hence, we con-
cluded that both oxygen[17] and moisture[18] have a negative
effect on the conversion of the Michael addition of acetalde-
hyde to trans-b-nitrostyrene.[19]
Encouraged by the results obtained with this dual catalyt-
ic system, we decided to test the generality of this concept
with different substrates, and the results are shown in
Table 3.[20] It was established that the system was tolerant to
b-nitrostyrenes bearing o-fluoro, o-chloro, and o-bromo sub-
stituents (Table 3, entries 2–4), m- and p-chloro substituents
being also well tolerated (entries 5 and 6). Electron-rich ni-
Entry
Acidic cat.
Solv.
Conv. [%][b]
ee [%][c]
1
–
CH2Cl2
CH2Cl2
CH2Cl2
dioxane
THF
MeCN
CH2Cl2
CH2Cl2
CH2Cl2
CH2Cl2
CH2Cl2
CH2Cl2
CH2Cl2
CH2Cl2
CH2Cl2
0
5
–
–
2[d]
3[d]
4[d]
5[d]
6[d]
7
pTsOH (10%)
2 (10%)
2 (10%)
2 (10%)
2 (10%)
2 (0.5%)
2 (1%)
42
15
10
32
45
41
46
47
40
69
91
35
55
90
90
90
90
90
90
90
91
90
90
91
90
91
8
9
10
11
2 (5%)
2 (10%)
2 (20%)
2 (10%)
2 (10%)
2 (10%)
2 (10%)
12[e]
13[e,f]
14[e,g]
15[e,h]
[a] Reactions were carried out with trans-b-nitrostyrene (0.1 mmol),
paraldehyde (0.33 mmol) in presence of 10 mol% catalyst 1, and
a
teabag with the acidic catalyst 2 in 0.5 mL CH2Cl2 unless otherwise
noted; [b] conversion was measured by 1H NMR spectroscopy; [c] ee was
measured by chiral HPLC analysis; [d] catalyst 2 was used without
teabag; [e] 20 mol% of catalyst 1 was used; [f] reaction was carried out
in a glove box in degassed anhydrous CH2Cl2; [g] 10 equivalents of water
were added; [h] oxygen was bubbled into the reaction mixture for 10 min
at the beginning.
Chem. Eur. J. 2013, 00, 0 – 0
ꢀ 2013 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
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