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for o-TA)9 (Fig. 2). o-TAs gave the highest conversion with (S)-a-MBA, 80 mL of 20 mM phosphate buffer (pH 7.0) containing 10 mM
and o-TAPO gave higher conversion (56.1%) than that of o-TABG 2a, 100 mM (S)-a-MBA, and 0.1 mM PLP using purified o-TAPO
(25.3%). Thus, (S)-a-MBA was selected as the best amino donor for (8 mg), and carefully 40 mL of iso-octane was added to 80 mL of
the asymmetric synthesis. When asymmetric synthesis was carried the aqueous reaction mixture. After 24 h of reaction, HPLC
out with 100 mM 2a, 100 mM (S)-a-MBA and o-TAPO (1 mg mLÀ1), analysis showed 93% conversion with 499% ee. 1a was isolated
the conversion was o3% after 24 h of reaction. Therefore, the from this reaction with 38% yield (ESI†).
substrate inhibition of o-TA by 2a was examined with 50 mM
In conclusion, enantiomerically pure (R)- and (S)-g-amino
(S)-a-MBA and various concentrations of 2a (0–100 mM) (Fig. S3, acids (499% ee) were produced using o-TAs through kinetic
ESI†). The initial reaction rates of o-TAPO and o-TABG were the resolution and asymmetric synthesis respectively. The present
highest at 5 mM 2a, and thereafter decreased with an increase in study demonstrates the high potentiality of o-TA reaction for
the concentration of 2a. In the presence of 10 mM 2a, o-TAPO the production of chiral g-amino acids. We are currently devel-
and o-TABG showed, respectively, 74 and 87% activities of those oping an asymmetric synthesis method to overcome product
with 5 mM 2a.
inhibition by using a coupling reaction.
Next, the asymmetric syntheses were carried out with 10 mM
This research was partially supported by Basic Science
2a due to severe substrate inhibition at higher concentration of Research Program through the National Research Foundation
2a (410 mM). Here, (S)-a-MBA was used as the amino donor for of Korea (NRF) funded by the Ministry of Education, Science and
the asymmetric synthesis of g-amino acids. The product inhibi- Technology (2013R1A2A2A01068013). And this research was
tion by acetophenone (deaminated product of a-MBA) is well partially supported by a grant (A10301712131560200) of Global
reported.9 To overcome the product inhibition by acetophenone, a Cosmetics R&D Project, Ministry of Health & Welfare, Korea.
biphasic reaction system with iso-octane was introduced (Fig. S4,
ESI†).14,16 In the biphasic system, g-amino acid (1a), g-keto acid (2a),
and (S)-a-MBA existed in the aqueous solution due to their
Notes and references
´˜
electric charges at neutral pH while the inhibitory acetophenone
gets transferred to the iso-octane layer. In the biphasic reaction
system, the biphasic mixture was gently shaken in a shaking
incubator with 250 rpm at 37 1C. As expected, the biphasic
reaction system gave higher conversion of the product (97%)
than the monophasic reaction system (80%). Subsequently,
asymmetric syntheses of various g-amino acids were carried
out in monophasic and biphasic systems (Table 2). Both systems
gave enantiomerically pure (S)-g-amino acids (499% ee). For all
the substrates, o-TAPO gave higher conversion than o-TABG,
which indicates that o-TAPO is a more suitable catalyst than
o-TABG for the asymmetric synthesis of g-amino acids. In most
of the cases, the biphasic system gave a higher conversion. It is
notable that 1f and 1g were less reactive substrates for the
kinetic resolution, but in asymmetric synthesis, the conversion
of 2f and 2g with o-TAPO was higher than other substrates.
Finally a preparative scale reaction was carried out at 37 1C in
1 For a review, see: M. Ordonez and C. Cativiela, Tetrahedron: Asymmetry,
2007, 18, 3–99.
2 K. Stratmann, D. L. Burgoyne, R. E. Moore and G. M. L. Patterson,
J. Org. Chem., 1994, 59, 7219–7226.
3 G. R. Pettit, Y. Kamano, C. L. Herald, A. A. Tuinman, F. E. Boettner,
H. Kizu, J. M. Schmidt, L. Baczynskyj, K. B. Tomer and R. J. Bontems,
J. Am. Chem. Soc., 1987, 109, 6883–6885.
4 Y. Kato, N. Kusetani, S. Matsunaga, K. Hashimoto and T. Furuya,
J. Am. Chem. Soc., 1986, 108, 2780–2781.
5 For selected examples, see: (a) K. Akagawa and K. Kudo, Angew.
Chem., 2012, 124, 12958–12961 (Angew. Chem., Int. Ed., 2012, 51,
12786–12789); (b) L.-T. Shen, L.-H. Sun and S. Ye, J. Am. Chem. Soc.,
2011, 133, 15894–15897; (c) H. Y. Bae, S. Some, J. H. Lee, J.-Y. Kim,
M. J. Song, S. Lee, Y. J. Zhang and C. E. Song, Adv. Synth. Catal.,
2011, 353, 3196–3202; (d) Y. Zhu, S. Khumsubdee, A. Schaefer and
K. Burgess, J. Org. Chem., 2011, 76, 7449–7457; (e) C. Shao, H.-J. Yu,
N.-Y. Wu, P. Tian, R. Wang, C.-G. Feng and G.-Q. Lin, Org. Lett.,
2011, 13, 788–791; ( f ) S. E. Park, E. H. Nam, H. B. Jang, J. S. Oh,
S. Some, Y. S. Lee and C. E. Song, Adv. Synth. Catal., 2010, 352,
2211–2217; (g) M. Furutachi, S. Mouri, S. Matsunaga and
M. Shibasaki, Chem. – Asian J., 2010, 5, 2351–2354.
6 K. M Koeller and C. H. Wong, Nature, 2001, 409, 232–240.
7 For selected Reviews see: (a) W. Leuchtenberger, K. Huthmacher
and K. Drauz, Appl. Microbiol. Biotechnol., 2005, 69, 1–8; (b) J. M.
Clemente-Jimenez, S. Martınez-Rodrıguez, F. Rodrıguez-Vico and
F. J. Heras-Vazquez, Recent Pat. Biotechnol., 2008, 2, 35–46.
´
´
´
´
Table 2 Asymmetric synthesis of g-amino acids
´
¨
8 For selected examples, see: (a) H. Groger, H. Trauthwein,
o-TAPO
o-TABG
S. Buchholz, K. Drauz, C. Sacherer, S. Godfrin and H. Werner, Org.
Biomol. Chem., 2004, 2, 1977–1978; (b) G. Cardillo, A. Tolomelli and
C. Tomasini, Eur. J. Org. Chem., 1999, 155–161; (c) D. Li, S. Cheng,
D. Wei, Y. Ren and D. Zhang, Biotechnol. Lett., 2007, 29, 1825–1830;
(d) T. Heck, D. Seebach, S. Osswald, M. K. J. ter Wiel, H.-P. E. Kohler
and B. Geueke, ChemBioChem, 2009, 10, 1558–1561; (e) A. Liljeblad
and L. T. Kanerva, Tetrahedron, 2006, 62, 5831–5854; ( f ) W. Szymanski,
B. Wu, B. Weiner, S. de Wildeman, B. L. Feringa and D. B. Janssen,
J. Org. Chem., 2009, 74, 9152–9157; (g) J. Rehdorf, M. D. Mihovilovic
and U. T. Bornscheuer, Angew. Chem., Int. Ed., 2010, 49, 4506–4508.
9 For selected reviews, see: (a) D. Koszelewski, K. Tauber, K. Faber and
W. Kroutil, Trends Biotechnol., 2010, 28, 324–332; (b) M. Hohne and
U. T. Bornscheuer, ChemCatChem, 2009, 1, 42–51; (c) M. S. Malik,
E. S. Park and J. S. Shin, Appl. Microbiol. Biotechnol., 2012, 94,
1163–1171; (d) S. Mathew and H. Yun, ACS Catal., 2012, 2, 993–1001;
(e) W. Kroutil, E. M. Fischereder, C. S. Fuchs, H. Lechner, F. G. Mutti,
D. Pressnitz, A. Rajagopalan, J. H. Sattler, R. C. Simon and E. Siirola,
Org. Process Res. Dev., 2013, 17, 751–759.
Monophasica
Biphasicb
Conv. eeS
Monophasic
Conv. eeS
Biphasic
Conv. eeS
Conv.
Sub. [%]
eeS
[%]
[%]
[%]
[%]
[%]
[%]
[%]
2a
2b
2c
2d
2e
2f
77.6
75.1
72.1
72.9
52.7
85.3
99.9
499
499
499
499
499
499
499
95.8
94.3
91.0
88.5
67.5
99.0
99.9
499 14.0
499 17.3
499 14.7
499
499
499
499 23.0
499 17.2
499 27.7
499 14.5
499
499 23.4
499 57.6
499
499
499
499
3.21
5.10
1.02
8.45 499
499
499
2g
499 48.9
a
Enzyme reactions were carried out at 37 1C in 1 mL of 200 mM Tris/
HCl buffer (pH 7.0) containing 10 mM substrate, 20 mM (S)-a-MBA,
0.1 mM PLP for 36 h by using o-TAPO (0.34 mg mLÀ1) or o-TABG
(0.68 mg mLÀ1); conv. and ee were determined by HPLC (see the ESI). b 1 mL
of iso-octane was added to 1 mL of the aqueous reaction mixture.
12682 | Chem. Commun., 2014, 50, 12680--12683
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