1
632
T. Osawa et al. / Tetrahedron: Asymmetry 25 (2014) 1630–1633
branching (2° group) led to 96–80% conversion, depending upon
the alkyl chain length. However, raising the temperature to
definite enantioface-selective fixation of the prochiral substrate
for the unidirectional approach of activated hydrogen.
1
10 °C significantly increased the conversion in almost all
examples. The sterically more demanding t-Bu group (3° group)
considerably decelerated the reaction down to 64% conversion at
3
. Conclusion
1
10 °C. In sharp contrast, Raney Ni-based catalysts are known to
In conclusion, high enantioselectivities of up to 94% have been
give almost identical conversions of 95–98%, irrespective of the
substrate structure. These observations could be attributed to
the difference in surface morphology between the Ni powder
achieved in enantiodifferentiating heterogeneous catalysis over
chirally modified Ni and by judicious choice of the prochiral sub-
strate. These results pave the way to the facile industrial produc-
tion of biologically important enantiopure hydroxybutyrate
derivatives.
3
4
2
6
3
5
and Raney Ni, which leads to the structural selectivity due to
the distinct accessibility of substrate to the catalyst surface where
the corresponding hydrogenation reaction takes place. This conclu-
sion is compatible with the hydrogenation mechanism proposed
previously for tartaric acid/NaBr-modified Ni catalyst,19 in which
the substrate is held near the catalyst surface through hydrogen-
bonding interactions with tartaric acid anchored to the Ni surface.
The effect of the alkyl chain length and branching on enantiose-
lectivity is somewhat less pronounced but is noticeable. In
particular, the ee value was appreciably improved from the original
4. Experimental
Nickel powders (5 lm) purchased from Aldrich were directly
subjected to chiral modification without any pretreatment, such
as hydrogen activation. The chiral modification was performed
under the conditions optimized previously for this type of cata-
2
6
8
9–91% for Me to 92–94% upon elongation to Et and to 91–93%
lyst.
Thus, the non-activated nickel powders (0.5 g) were
3
upon further elongation to n-Pr and n-Bu. This trend may be attrib-
uted to the ambivalent roles of the steric bulk in enhancing the
enantiomeric face-selectivity upon complexation and subsequent
hydrogenation and also discouraging the tight complexation with
tartaric acid, which would be balanced when the Et ester is used.
This view may be rationalized by the fact that the more bulky
i-Pr group yields a reduced 91–92% ee, while the more bulky t-Bu
ester gives the lowest 72–84% ee. For secondary branched short
alkyl esters, no such unfavorable effect on the enantioselectivity
was observed. Thus, the n-Pr and i-Pr esters afforded comparable
immersed in an aqueous solution (50 cm ) of (R,R)-tartaric acid
(0.5 g) and NaBr (2.0 g) at 100 °C, the pH of which was pre-adjusted
to 3.2 with an aqueous 1 M NaOH solution. NaBr was added to the
modification solution to block the non-enantiodifferentiating sites
of tartaric acid/Ni catalyst, thus preventing the generation of race-
mic products. After immersion for 1 h, the modification solution
was removed by decantation and the catalyst was successively
washed once with deionized water (10 cm ), twice with methanol
3
9
3
3
3
(25 cm ), and twice with tetrahydrofuran (THF) (10 cm ). The
modified catalyst was added to a mixture of alkyl acetoacetate
(43 mmol for methyl ester and 21.5 mmol for other esters), acetic
9
1–92% ee, while i- and s-Bu esters gave slightly higher 92–94%
3
and 91–93% ee, respectively. The introduction of the aromatic
substituent also reduces the ee value down to 88–89%, indicating
that the p-interactions do not play any significant role in the stabil-
ization of the supramolecular complex or the asymmetric attack of
an activated hydrogen molecule, while excessive bulk discourages
the prochiral faceselectivity of the supramolecular complex. This
bulkiness-controlled enantioselectivity is in contrast to the almost
acid (0.1 g), and THF (10 cm ) placed in an autoclave equipped
with a magnetically coupled mechanical stirrer. The hydrogenation
was run for 20 h at 100 or 110 °C and at a hydrogen pressure of
9 MPa. The hydrogenation product, a mixture of alkyl (R)- and
(S)-3-hydroxybutyrates, was isolated from the reaction mixture
by distillation. The conversion was determined by gas-liquid chro-
matography (GLC) on a GL Science model GC-4000 equipped with a
CP Chirasil DEX-CB capillary column (0.25 mm  25 m) at 90 °C,
while the enantioselectivity was determined by chiral GLC after
acetylation of the reaction product using acetyl chloride and pyri-
dine. A portion of the acetylated sample was subjected to the chiral
GLC analysis on a CP Chirasil DEX-CB column (0.25 mm  25 m)
operated at 90 °C. The ee value was calculated from the peak inte-
gration of the corresponding enantiomer peaks. The reproducibility
of the ee value was found to be within ±2%.
invariant ee values (Dee = ±2%) regardless of the ester structure,
which have been reported for the Raney Ni catalyst (Table 1).
Furthermore, the sensitivity to steric bulk observed for the Ni pow-
der-based catalyst allowed for considerable enhancement of the
enantiodifferentiating performance of catalytic heterogeneous
hydrogenation by 6–7% in comparison with the conventional
Raney Ni-based catalysts.
So far, there have been several models proposed for the inter-
mediate host-guest complex of chiral tartaric acid with prochiral
acetoacetate substrate on the metallic surface.36 For example,
according to Tai’s mechanism, the two hydroxyl groups of the tar-
taric acid molecule attached to the Ni surface interact with two
carbonyl groups of the b-ketoester via hydrogen bonding.3 Mean-
while, Osawa et al. proposed a different type of interaction
between tartaric acid and b-ketoester. In this case the carbonyl
group of the b-ketoester interacts with one hydroxyl group of
tartaric acid, while the ester carbonyl moiety is bonded to sodium
ion, which is an important component of the reaction mixture to
ensure high enantioselectivity of hydrogenation.38 However, none
of these reports explicitly explain the role of substrate bulk in
general and in particular the effect of the ester substituent on
the catalytic efficiency. Although the specific host–guest
interaction mechanism and the role of the ester group in the
activated catalyst complex are yet to be understood in detail, the
results obtained clearly indicate that the most plausible rationale
of the observed behavior is a structural ‘key-and-lock’ principle
based upon the geometrical complementarity between the
adsorbed tartaric acid and acetoacetate derivative resulting in the
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