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A. Wolfson et al. / Tetrahedron: Asymmetry 17 (2006) 2043–2045
Table 2. Comparison of the performance of IBY in the asymmetric reduction of ethyl acetoacetate in recyclable reaction media
2045
Medium
Ethyl acetoacetate (g)
Energy source (g)
IBY (g)
t (h)
Conversion (%)
Isolated yield (%)
ee (%)
Water
Glycerol
Ionic liquid15
Fluorous phase16
1
1
1.3
0.25
5
5
7.9
1
10
10
10
2.5
20
48
72
41
100
99
70
92
90
—
25
99
99
95
95
100
The product extractions were carried out in the presence of
the yeast cells since part of the product existed in the cells.
The highest extraction yields (>90%) were obtained with
ethyl acetate, which is relatively less toxic than other gly-
cerol immiscible solvents.17 The product extractions were
completed in the presence of the yeast cells, since part of
the product existed in the cells.
ral carbonyl compounds with baker’s yeast. Both activity
and enantioselectivity were high and competitive with the
reactions in water. IBY showed higher activity than FBY
with the same enantioselectivity. However, it should be
taken into account that although the immobilization proce-
dure is simple it requires some effort and time. High
products extraction yields were obtained.
The performance of IBY in the asymmetric reduction of
ethyl acetoacetate in various green solvents was then com-
pared (Table 2). The results in Table 2 illustrate that per-
forming the reaction in glycerol is advantageous over
ionic liquids or fluorous media as it is more active and
enantioselective and it affords higher product isolation
yield by simple extraction.
References
1. Tsachen, D. M.; Fuentes, L. M.; Lynch, J. E.; Laswell, W. L.;
Volante, R. P.; Shinkai, I. Tetrahedron Lett. 1988, 29, 2779.
2. Mori, K. Tetrahedron 1989, 45, 3233.
3. Noyori, R. Asymmetric Catalysis in Organic Synthesis; John
Wiley: New York, 1994.
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Tetrahedron: Asymmetry 2003, 14, 2659.
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7. Rotthaus, O.; Kruger, D.; Demuth, M.; Schaffner, K.
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Tetrahedron 1997, 53, 935.
8. Qun, J.; Shanjing, Y.; Lehe, M. Enzyme Microb. Technol.
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A.; Heijnen, J. J. Enzyme Microb Technol. 2002, 31, 656.
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R. J.; Fournier, A. Appl. Microbiol. Biotechnol. 1992, 38, 39.
12. Hulst, A. C.; Tramper, J.; Van’t Riet, K.; Westerbeek, J. M.
M. Biotechnol. Bioeng. 1985, 27, 870.
As previously mentioned, one of the advantages of using an
organic solvent instead of water in yeast catalyzed enantio-
selective reductions is the ease of isolation of the prod-
ucts.13,18 The asymmetric reduction of ethyl acetoacetate
with FBY for example, was successfully performed in var-
ious organic solvents.7,18 Employing light petroleum as the
solvent resulted in 70% product isolation yield. The separa-
tion procedure involved yeast filtration and wash, solvent
evaporation under reduced pressure and bulb to bulb distil-
lation. Conversely, using glycerol as the reaction media
allowed simple extraction of the product with ethyl acetate
and after removal of the solvent at room temperature un-
der reduced pressure, the isolation yield was 90%. Hence,
not only is glycerol greener than light petroleum and other
hydrocarbons but the separation procedure is simpler and
the product isolation yield is also higher.
13. Medson, C.; Smallridge, A. J.; Trewhella, M. A. Tetrahedron:
Asymmetry 1997, 7, 1049.
Finally, the enantioselective reductions of simple ketones in
a yeast fermenting aqueous system usually results in mod-
erate enantioselectivities.19 This is probably due to the fact
that the ketones are unnatural substrates for alcohol dehy-
drogenase from baker’s yeast. Reduction of 2-hexanone in
an ionic liquid yielded higher activity and similar enantio-
selectivity when compared with an aqueous system
(% ee = 80).15 Performing the reduction of 2-octanone
and 2-butanone in glycerol resulted in much higher enantio-
selectivities (% ee >97). The separation of 2-butanol from
an aqueous system is problematic since it forms azeotropic
mixture with water. Employing glycerol as the solvent
allowed the simple distillation of the alcohol with high iso-
lation yield due to the low vapour pressure of glycerol.
14. Johns, M. K.; Smallridge, A. J.; Trewhella, M. A. Tetra-
hedron Lett. 2001, 42, 4261.
15. Howarth, J.; James, P.; Dai, J. Tetrahedron Lett. 2001, 42,
7517.
16. Yajima, A.; Naka, K.; Yabuta, G. Tetrahedron Lett. 2004, 45,
4577.
17. The representative procedure for methyl acetoacetate reduc-
tion with FBY and IBY in glycerol: 10 g of FBY (SIGMA,
type II) or 50 g of IBY (prepared from 10 g of FBY as
described in 10) was added to a mixture of 50 mL of glycerol
(99% purity, purchased from Frutarom Ltd) in a 250 mL
bottle and shaken for 30 min. Then 5 g of energy source was
added and the bottle was shaken for 10 min before 1 g of
methyl acetoacetate was added. The bottle was shaken at
300 rpm for 96 h at 37 ꢁC. At the end of the reaction, the
products were extracted with ethyl acetate (3 · 50 mL). The
conversion and the enantiomeric excess of the product were
determined by GC analysis with Astec, Chiraldex G-TAꢂ
(30 m · 0.25 mm, 0.25 lm thickness).
3. Conclusions
18. Jayasinghe, L. Y.; Kodituwakku, D.; Smallridge, A. J.;
Trewhella, M. A. Bull. Chem. Soc. Jpn. 1994, 67, 2528.
19. MacLeod, R.; Prosser, H.; Fikentscher, L.; Lanyi, J.; Mosher,
H. S. Biochemistry 1964, 3, 838.
In conclusion, glycerol, which is a renewable and biode-
gradable green solvent was employed for the first time as
a reaction medium in the asymmetric reduction of prochi-