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K. Tanaka, K. Fukase
LETTER
as a single isomer (entry 5).16 Finally, the selective reduc-
tion of galactose derivative 4 gave the 6-O-benzyl deriva-
tive 10 in 91% yield (entry 6).17 It is worth mentioning
that the established microfluidic reaction reproducibly
provided the O-benzylated compounds 5–10 in greater
than 90% yields in all cases, out of the three experiments
performed in each entry of Table 1. Furthermore, no spe-
cial dehydration procedures, such as pre-drying of the re-
action apparatus and the solvents by molecular sieves, are
necessary, making the present microflow reaction a prac-
tical procedure in large-scale syntheses.18
(10) For recent applications, see: (a) Pennemann, H.; Hessel, V.;
Loewe, H. Chem. Eng. Sci. 2004, 59, 4789. (b) Jahnisch,
K.; Hessel, V.; Loewe, H.; Baerns, M. Angew. Chem. Int. Ed.
2004, 43, 406. (c) Nagaki, A.; Togai, M.; Suga, S.; Aoki, N.;
Mae, K.; Yoshida, J.-I. J. Am. Chem. Soc. 2005, 127, 11666.
(d) Ratner, D. M.; Murphy, E. R.; Jhunjhunwala, M.;
Snyder, D. A.; Jensen, K. F.; Seeberger, P. H. Chem.
Commun. 2005, 578.
(11) A new micromixing device, ‘Comet X-01’ (Techno
Applications Co., Ltd., 34-16-204, Hon, Denenchofu, Oota,
Tokyo 1450072, Japan), was used. It exhibited much
superior mixing efficiency to the simple T-shape mixer and
similar efficiency to the IMM micromixer for acid-catalyzed
reaction, such as dehydration (data not reported). This new
device is well suited for a large-scale synthesis and for
establishing a micro chemical plant. The detailed structure
and mixing system will be reported elsewhere.
In summary, we have realized an efficient microfluidic
procedure for the reductive opening of the sugar 4,6-O-
benzylidene acetals. It is of note that the continuous
microflow reaction established in Table 1 can be readily
applied to large-scale reactions. The present microflow
process is now being utilized in our laboratory for the
synthesis of complex oligosaccharides.
(12) Vera-Ayoso, Y.; Borrachero, P.; Cabrera-Escribano, F.;
Carmona, A. T.; Gomez-Guillen, M. Tetrahedron:
Asymmetry 2004, 15, 429.
(13) The products ratio of 4- and 6-O-benzyl derivatives was
same as those obtained by batch reaction.
(14) Tanaka, S.; Takashina, M.; Tokimoto, H.; Fujimoto, Y.;
Tanaka, K.; Fukase, K. Synlett 2005, 2325.
Acknowledgment
(15) Sakai, Y.; Oikawa, M.; Yoshizaki, H.; Ogawa, T.; Suda, Y.;
Fukase, K.; Kusumoto, S. Tetrahedron Lett. 2000, 41, 6843.
(16) Inamura, S.; Fukase, K.; Kusumoto, S. Tetrahedron Lett.
2001, 42, 7613.
(17) El-Shenawy, H.; Schuerch, C. Carbohydr. Res. 1984, 131,
227.
We acknowledge Dr. Yukio Matsubara, the general manager of
Techno Applications Co., Ltd., Tokyo, Japan, for generously provi-
ding us with a new micromixer device, ‘Comet X-01’. The present
work was financially supported in part by Grant-in-Aid for Scienti-
fic Research No. 17310128 and No. 18850014 from the Japan
Society for the Promotion of Science and also by The Mitsubishi
Foundation, Research Grants in the Natural Sciences.
(18) Microfluidic Reaction; Typical Procedure: A solution of
BF3·OEt2 (3 mL, 23.7 mmol, 1.0 M) in CH2Cl2 (23.7 mL)
was injected in advance to the micromixer by using a syringe
pump at a flow-rate of 0.5 mL/min. Subsequently, a solution
of benzylidene acetal 1 (1 g, 2.69 mmol, 0.1 M) and Et3SiH
(4.3 mL, 26.9 mmol, 1.0 M) dissolved in CH2Cl2 (26.9 mL)
was also injected to the micromixer by another syringe pump
at the flow rate of 0.5 mL/min and mixed at 0 °C. After the
reaction mixture was allowed to flow at r.t. for an additional
45 s through a Teflon reactor tube (F = 1.0 mm, l = 0.9 m),
the mixture was quenched by pouring it to a sat. NaHCO3
solution at 0 °C. It took about 7 min to consume 1 g of the
substrate 1 under above conditions. The mixture was
extracted with EtOAc, washed with brine, dried over
Na2SO4, filtered, and concentrated in vacuo to give the crude
product. The residue was purified by preparative TLC on
silica gel (50% EtOAc in hexane) to afford 5 (935 mg, 93%).
The conditions established herein can be readily applied to
the scale-up synthesis simply by preparing the stock
solutions of substrate and reagents and pumping them
continuously into the micromixer.
References and Notes
(1) Greene, T. W.; Wuts, P. G. M. Protective Groups in Organic
Synthesis; John Wiley and Sons, Inc.: New York, 1991.
(2) DeNinno, M. P.; Etienne, J. B.; Duplantier, K. C.
Tetrahedron Lett. 1995, 36, 669.
(3) Oikawa, M.; Liu, W.-C.; Nakai, Y.; Koshida, S.; Fukase, K.;
Kusumoto, S. Synlett 1996, 1179.
(4) Garegg, P. J.; Hultberg, H.; Wallin, S. Carbohydr. Res.
1982, 108, 97.
(5) Johansson, R.; Samuelsson, B. J. Chem. Soc., Perkin Trans.
1 1984, 2371.
(6) Guindon, Y.; Girard, Y.; Berthiaume, S.; Gorys, V.;
Lemieux, R.; Yoakim, C. Can. J. Chem. 1990, 68, 897.
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(8) Fugedi, P.; Liptak, A.; Nanasi, P.; Szejtli, J. Carbohydr. Res.
1982, 104, 55.
(9) For representative reviews, see: (a) Microreaction
Technology; Ehrfeld, W., Ed.; Springer: Berlin, 1998.
(b) Microsystem Technology in Chemistry and Life Sciences;
Manz, A.; Becker, H., Eds.; Springer: Berlin, 1998.
(c) Ehrfeld, W.; Hessel, V.; Lowe, H. Microreactors; Wiley-
VCH: Weinheim, 2000. (d) Hessel, V.; Hardt, S.; Lowe, H.
Chemical Micro Process Engineering; Wiley-VCH:
Weinheim, 2004. (e) Yoshida, J.-I.; Suga, S.; Nagaki, A. J.
Synth. Org. Chem. Jpn 2005, 63, 511.
Synlett 2007, No. 1, 164–166 © Thieme Stuttgart · New York