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RSC Advances
Table 1 Asymmetric hydrogenation of b-keto esters
This maybe because the catalyst still contains trace amounts of
Lewis acid FeCl3, which may accelerate the side reaction,
although the material have been thoroughly washed during its
preparation process. Meanwhile, the reuse property of Ru/KAP-1
catalyst was preliminary explored, and it could be reused for
four times with the high yield (higher than 99.5%) and a slight
decrease on ee value (from 96.0% to 94.7%) (Fig. 2).
Entry Catalyst
R
S/Cb
Yieldc (%) eec (%)
1d
Ru/KAP-1 R1 ¼ R2 ¼ Me
Ru/KAP-2 R1 ¼ R2 ¼ Me
Ru/KAP-3 R1 ¼ R2 ¼ Me
Ru/KAP-1 R1 ¼ R2 ¼ Me
Ru/KAP-2 R1 ¼ R2 ¼ Me
Ru/KAP-3 R1 ¼ R2 ¼ Me
Ru/KAP-1 R1 ¼ R2 ¼ Me
Ru/KAP-1 R1 ¼ R2 ¼ Me
Ru/KAP-1 R1 ¼ iPr, R2 ¼ Me
Ru/KAP-1 R1 ¼ Me, R2 ¼ et
Ru/KAP-1 R1 ¼ Me, R2 ¼ iPr
1000 >99.5
96.4
95.7
94.8
97.0
94.1
96.8
97.0
97.9
96.4
98.7
94.0
94.8
Conclusions
2d
1000
1000
45.1
45.7
3d
In summary, a series of novel porous polymers (KAP-1, KAP-2,
KAP-3) with no-modied BINAP were successfully synthesized
by Friedel–Cras reaction for the rst time. These polymer-
supported catalysts demonstrated excellent activities and
enantioselectivities on the asymmetric hydrogenation of b-keto
esters. Further efforts are underway with a focus on reduction of
partly oxidized BINAP in knitting networks to improve the
stability of catalysts.
4a
1000 >99.5
1000 >99.5
1000 >99.5
4000 >99.5
6000 >99.5
5a
6a
7a
8e
9a
1000
91.9
10f
11g
12h
1000 >99.5
1000
96.5
90.9
Ru/KAP-1 R1 ¼ Me, R2 ¼ tBu 1000
a
Reaction conditions: 2 mL methanol, initial H2 pressure 2 MPa,
b
0.00086 mmol Ru with BINAP/Ru at 10, 80 ꢁC, 10 h. Molar ratio of
Acknowledgements
c
substrate to catalyst. Determined by GC on a Cyclosil-B capillary
d
e
f
g
column. 0.5 MPa H2. 4 mL methanol. 2 mL ethanol. 2 mL
This work was supported by the National Natural Science
Foundation of China (21303190).
isopropanol. h 2 mL t-butanol.
Notes and references
different catalytic activities. Abundant micropores are favour-
able for the complete contact between substrate and the cata-
lytically active sites, and the mesopores improved mass transfer
efficiency in heterogeneous catalysis.8b,10 It also showed that the
Ru/KAP-1 has more channels than the other two catalysts
through the TEM images. So, Ru/KAP-1 showed higher catalytic
activity than the other catalysts. The other reason for the high
activity and enantioselectivity of the catalyst could be attributed
to the incorporated BINAP in the polymer backbones, which
offered a uniform catalytic activity sites. Interestingly, when
a series of b-keto esters were catalysed by Ru/KAP-1 for asym-
metric hydrogenation, their corresponding alcohols were used
as the solvent rather than methanol. Otherwise trans-
esterication reaction could easily take place (entries 9–12).
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Fig. 2 Recycle of the Ru/KAPs-1 catalyst for the hydrogenation of
methyl acetoacetate. Reaction conditions: 4 mL methanol, initial H2
pressure 2 MPa, 0.00172 mmol Ru (S/C ¼ 1000), 80 ꢁC, 10 h.
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