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Y. Kuroiwa et al. / Tetrahedron Letters 51 (2010) 6294–6297
Table 4
Table 6
The removal rate of water from an ionic liquid under reduced pressure conditions
Recycling of C6mim[NTf2] for the glycosylation of 4 with 2 under reduced pressure
conditions
H2O
HNTf2, C6mim[NTf2]
4
+
2
3
+
C6mim[NTf2]
H2O
C6mim[NTf2]
º
70 C, 4.0 mmHg,
70 oC, 4.0 mmHg
(1.1 eq.)
30 min
Entry
Time (min)
Remaining H2Oa (%)
Entry
Additive/HNTf2 (equiv)
Yield (%) of 3
a
/b ratioa
1
2
0
5
100
0
1
2
3
4
1st run
1st reuse
2nd reuse
3rd reuse
—
0
0
0.05
82
69
52
84
65/35
52/48
46/54
68/32
The quantity was determined by 1H NMR analysis.
a
a
a/b ratios were determined by HPLC analysis.
With these favorable results in hand, we next carried out the
glycosylation of 4 with the alcohols 5–8 (1.1 equiv), including the
poorly reactive secondary alcohols 6, 7, and 8, to examine the
scope and limitations of the reaction. These results are summa-
rized in Table 5. It was found that the glycosylations of 4 with just
slightly more than an equimolar amount (1.1 equiv) of these glyco-
syl acceptors proceeded smoothly in C6mim[NTf2]/HNTf2
(0.1 equiv) at 70 °C and 4.0 mmHg for 30 min, as well as with 2,
to afford the corresponding glycosides 9–12 in good yields (entries
1–5). These results clearly indicated that the use of a non-volatile
acid-IL under reduced pressure conditions provided significant
advantages for the direct glycosylation of inactive glycosyl donors
without the need for an excess quantity of glycosyl acceptor.
Finally, the reusability of the acid-IL C6mim[NTf2]/HNTf2 for
the glycosylation of 4 with 2 under reduced pressure conditions
was investigated. First, we attempted to reuse the recovered
C6mim[NTf2]/HNTf2 after extraction of the products from the
reaction mixture with a 5:1 mixture of hexane and EtOAc fol-
lowed by drying. It was found, however, that the chemical yield
gradually decreased as the recycle number increased (ꢀ15%
decrease for each reaction Table 6, entries 1–3) due to loss of
the protic acid HNTf2 during the glycosylation reaction at 70 °C
and 4.0 mmHg for 30 min. Therefore, we next examined the reuse
of the acid-IL after addition of HNTf2 (0.05 equiv) to the recovered
solvent. It was found that the efficiency of C6mim[NTf2]/HNTf2
thus recovered was identical with that of the freshly prepared
system and could be reused for the glycosylation under reduced
pressure conditions without any loss in efficiency (entry 4).
In conclusion, we have developed a novel O-glycosylation of
inactive glycosyl donors under reduced pressure conditions using
a reusable ionic liquid containing a protic acid without the need
for excess amounts of glycosyl acceptors. Furthermore, the effect
of the reduced pressure conditions on the efficiency of the glyco-
sylation was clearly demonstrated. Although this method pre-
sented herein is still not applicable for glycosylations using
volatile glycosyl acceptors, and the stereoselectivity is not satisfac-
tory, the results achieved with this simple and environmentally be-
nign protocol should open a novel green process and find wide
application in the synthesis of biomolecules and functional materi-
als containing carbohydrate structures. Further studies along this
line are currently in progress.
Table 5
Glycosylation of
4 with glycosyl acceptors 5–8 using C6mim[NTf2]/HNTf2 under
reduced pressure conditions
Acknowledgments
OBn
O
HNTf2 (0.1 eq. to IL)
C6mim[NTf2] (0.2 M for 4)
This research was supported by the High-Tech Research Center
Project for Private Universities: Matching Fund Subsidy, 2006–
2011, from the Ministry of Education, Culture, Sports, Science
and Technology of Japan (MEXT).
BnO
BnO
HO
5-8
R
4
+
º
70 C, 4.0 mmHg,
BnO
9-12
OR
(1.1 eq.)
30 min
Supplementary data
OBn
R=
12
Supplementary data (experimental procedures and character-
ization of new compounds) associated with this article can be
5, 9
6, 10
References and notes
1. (a) Toshima, K.; Tatsuta, K. Chem. Rev. 1993, 93, 1503; (b) Toshima, K.; Sasaki,
K.. In Comprehensive Glycoscience; Kamerling, J. P., Boons, G.-J., Lee, Y. C., Suzuki,
A., Taniguchi, N., Vorangen, A. G. J., Eds.; Elsevier: Oxford, 2007; Vol. 1, p 261.
2. Green Chemistry: Theory and Practice; Anastas, P. T., Warner, J. C., Eds.; Oxford
University Press: Great Britain, 1998.
7, 11
8, 12
3. Ionic Liquids in Synthesis; Wasserscheid, P., Welton, T., Eds.; Wiley-VCH:
Weinheim, 2002.
Entry
Acceptor
Product
Yield (%)
a
/b ratioa
4. For recent reviews of ionic liquids, see: (a) Baudequin, C.; Baudoux, J.; Levillain,
J.; Cahard, D.; Gaumont, A.-C.; Plaquevent, J.-C. Tetrahedron: Asymmetry 2003,
14, 3081; (b) Jain, N.; Kumar, A.; Chauhan, S.; Chauhan, S. M. S. Tetrahedron
2005, 61, 1015; Baudequin, C.; Baudoux, J.; Levillain, J.; Guillen, F.; Plaquevent,
J.-C.; Gaumont, A.-C. Tetrahedron: Asymmetry 2005, 16, 3921; (d) Muzart, J. Adv.
Synth. Catal. 2006, 348, 275; (e) Chowdhury, S.; Mohan, R. S.; Scott, J. L.
Tetrahedron 2007, 63, 2363; (f) Olivier-Bourbigou, H.; Magna, L.; Morvan, D.
Appl. Catal., A 2010, 373, 1.
1
2
3
4
5
2
5
6
7
8
3
9
10
11
12
82
73
70
65
57
65/35
60/40
65/35
63/37
65/35
a
a
/b ratios were determined based on isolated yields of both isomers.