Communications
Table 1: Catalytic enantioselective oxidation of sulfides with H2O2 and a
the catalysts and to determine which iron species is respon-
sible for the observed enantioselectivity.
chiral iron complex.[a]
Entry Ligand Sulfide 2
Sulfoxide Yield [%][b] ee [%][c] Config.[d]
1
2
3
4
5
1a
1b
1c
1d
1e
Ph-S-Me
(2a)
Ph-S-Me
(2a)
Ph-S-Me
(2a)
Ph-S-Me
(2a)
Ph-S-Me
(2a)
Ph-S-Me
(2a)
Ph-S-Et (2b) 3b
Ph-S-Bn (2c) 3c
p-ClPh-S-Me 3d
(2d)
p-BrPh-S-Me 3e
(2e)
3a
3a
3a
3a
3a
3a
27
15
27
30
36
40
26
13
23
55
59
51
(S)-(À)
(S)-(À)
(S)-(À)
(S)-(À)
(S)-(À)
(S)-(À)
Experimental Section
[Fe(acac)3] (7.1 mg, 0.02 mmol) and ligand 1 (0.04 mmol) were
dissolved in dichloromethane (1 mL) in a 10-mL flask, and the clear
red solution was stirred until it turned brown (15 min). A solution of
the sulfide (1 mmol) in dichloromethane (1 mL) was then added,
followed by the dropwise addition of aqueous H2O2 (30%; 1.2 mmol).
The flask was then capped and the reaction mixture was slowly stirred
at room temperature (approximately 150 rpm). After 16 h, the
aqueous layer was separated, and the organic layer was dried over
MgSO4, filtered, and the solvent removed in vacuo. The product was
then purified by flash chromatography on silica gel (pentane/diethyl
ether 1:1, then ethyl acetate). The enantiomeric excesses were
determined by HPLC on chiral stationary phases (Gynkotek appa-
ratus; UV detector UVD 170S (254 nm); 208C; flow rate
0.5 mLminÀ1 unless indicated otherwise). Retention times [min]:
(R)-3a 26.6, (S)-3a 31.7 (Chiralcel OD, heptane/iPrOH 9:1); (R)-3b
20.5, (S)-3b 25.7 (Chiralcel OD, heptane/iPrOH 9:1); (R)-3c 31.3,
(S)-3c 38.7 (Chiralcel OD, heptane/iPrOH 9:1); (S)-3d 23.2, (R)-3d
34.3 (Chiralcel OD, heptane/iPrOH 9:1); (S)-3e 26.1, (R)-3e 35.0
(Chiralcel OB-H, heptane/iPrOH 8:2, flow rate 0.4 mLminÀ1); (R)-3 f
44.2, (S)-3 f 49.7 (Chiralcel OJ, heptane/iPrOH 7:3); (+)-3g 38.9, (À )-
3g 43.5 (Chiralcel OD, heptane/iPrOH 9:1; optical rotation measured
in CHCl3).
6[e] 1e
7
8
9
1e
1e
1e
30
40
32
44
27
65
(S)-(À)
(S)-(À)
(S)-(À)
10
11
12
1e
1e
1e
41
21
44
78
90
70
(S)-(À)
(S)-(À)
(À)
p-NO2Ph-S- 3 f
Me (2 f)
2-Naphthyl- 3g
S-Me (2g)
[a] Reaction conditions: [Fe(acac)3] (0.02 mmol), ligand (0.04 mmol),
sulfide (1 mmol), aqueous H2O2 (30%; 1.2 mmol), CH2Cl2. [b] Yield of
isolated product. [c] The enantiomer ratios were determined by HPLC on
a chiral stationary phase. [d] The absolute configurations were assigned
by comparing optical rotations and HPLC elution orders with known
literature data. [e] Urea–H2O2 adduct (UHP, 1.2 mmol) was used instead
of aqueous H2O2.
Received: August 12, 2003 [Z52635]
Keywords: asymmetric catalysis · iron · oxidation · peroxides ·
.
sulfoxides
[1] a) R. A. Sheldon, Chem. Tech. 1994, 24, 38 – 47; b) see also: C.
Bolm, O. Beckmann, O. A. G. Dabard, Angew. Chem. 1999, 111,
957 – 959; Angew. Chem. Int. Ed. 1999, 38, 907 – 909.
of thioanisole (2a) (Table 1, entries 1–5). The highest enan-
tioselectivities were obtained with ligands derived from (S)-
tert-leucinol. In contrast to large substituents such as tert-butyl
(less than 23% ee for ligands 1b and 1c) on the aryl moiety,
halogen atoms such as Br or I (ligands 1d and 1e[10d]) increase
the enantioselectivity significantly (55 and 59% ee, respec-
tively; Table 1, entries 4 and 5).
[2] For a recent comparative assessment of asymmetric oxidations,
see: C. Bonini, G. Righi, Tetrahedron 2002, 58, 4981 – 5021.
[3] Efficient asymmetric sulfide oxidations are required in various
processes towards pharmaceutically relevant molecules. One of
the most important is the synthesis of the chiral sulfoxide,
omeprazole, which is one of the most sold drugs in the world
(sales in 2002: US$6.6 billion). For a summary of recent
developments and data, see: A. M. Rouhi, Chem. Eng. News
2003, 81(19), 56 – 61.
[4] For overviews on the use of H2O2 in oxidation reactions, see:
a) Catalytic Oxidations with Hydrogen Peroxide as Oxidant (Ed.:
G. Strukul), Kluwer Academic, Dordrecht, 1992; b) C. W. Jones,
Applications of Hydrogen Peroxide and Derivatives, Royal
Society of Chemistry, Cambridge, 1999; c) B. S. Lane, K.
Burgess, Chem. Rev. 2003, 103, 2457 – 2473.
[5] a) H. B. Kagan, T. Luukas in Transition Metals for Organic
Synthesis (Eds.: M. Beller, C. Bolm), Wiley-VCH, Weinheim,
1998, pp. 361 – 373; b) H. B. Kagan in Catalytic Asymmetric
Synthesis, 2nd ed. (Ed.: I. Ojima), Wiley-VCH, New York, 2000,
pp. 327 – 356; c) C. Bolm, K. Muꢀiz, J. Hildebrand in Compre-
hensive Asymmetric Catalysis (Eds.: E. N. Jacobsen, A. Pfaltz, H.
Yamamoto), Springer, Berlin, 1999, pp. 697 – 713.
[6] Recently, niobium and tungsten complexes have also been
involved in asymmetric sulfoxidation reactions: a) Nb: T.
Miyazaki, T. Katsuki, Synlett 2003, 1046 – 1048; b) W: V. V.
Takur, A. Sudalai, Tetrahedron: Asymmetry 2003, 14, 407 – 410.
[7] a) J. T. Groves, P. Viski, J. Org. Chem. 1990, 55, 3628 – 3634; b) Y.
Naruta, F. Tani, K. Maruyama, J. Chem. Soc. Chem. Commun.
1990, 1378 – 1380; c) Y. Naruta, F. Tani, K. Maruyama, Tetrahe-
The chiral iron/H2O2 system affords products with partic-
ularly high ee values in the oxidation of aryl methyl sulfides
(59–90% ee). Under the conditions described, no sulfones are
formed, which indicates that the enantioselectivities are a
direct result of the asymmetric sulfide oxidation and not of a
kinetic resolution by overoxidation of the resulting sulfox-
ide.[12] A limitation of the reported catalysis stems from the
fact that under the reaction conditions optimized to achieve
high enantioselectivities, significant amounts of the substrates
remain and the yields do not exceed 44%. All attempts to
reach higher sulfide conversions (by increasing the catalyst
loading and/or the amount of oxidant,[12] slow addition of the
oxidant, or performing the reaction under homogeneous
conditions[13]) afforded sulfoxides with lower ee values.
The results described herein, albeit not as good as those
already reported with chiral complexes of other metals,[5]
constitute the basis for a promising new approach and a
major step in the ascent of iron-catalyzed asymmetric
oxidation in general, and sulfoxidation in particular. Inves-
tigations are currently underway to improve the efficiency of
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ꢀ 2003 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Angew. Chem. Int. Ed. 2003, 42, 5487 –5489