Table 2. Asymmetric Hydroformylation of Styrene (St), Allyl Cyanide (AC), and Vinyl Acetate (VA) with Chiraphite, 1-7, and
Binaphosa
conversionb
regioselectivityc
(b/l) (St, AC, VA)
enantioselectivity
entry
1
ligand
T (°C)
(%) (St, AC, VA)
(% ee, configuration) (St, AC, VA)
Chiraphite
35
53.5, 67.2, 21.9
98.1, 100, 94.8
39.6, 95.1, 19.4
99.6, 100, 98.7
81.9, 99.6, 18.9
99.9, 100, 98.7
31.3, 57.9, 2.5
99.4, 100, 80.9
92.6, 99.6, 15.5
100, 100, 98.6
43.3, 61.1, 2.8
100, 100, 100
59.4, 86.7, 11.1
100, 100, 99.9
15.2, 23.4, 6.2
63.2, 99.9, 83.7
33.0, 49.3, 9.9
99.8, 99.9, 94.2
46.8, 6.7, 109.2
13.3, 6.1, 100.2
68.3, 15.9, 124.7
17.2, 10.8, 55.7
29.6, 12.2, 21.5
12.0, 10.5, 16.4
26.8, 5.4, 160.0
7.6, 5.3, 11.3
35.1, 6.5, 107.0
12.6, 7.1, 180.0
16.1, 5.3, 12.3
2.3, 4.2, 35.8
16.6, 5.0, 13.9
2.4, 4.0, 28.4
16.2, 5.0, 20.7
1.1, 3.4, 166.3
9.7, 2.7, 7.0
76.4 (S), 12.6 (R), 58.0 (S)
55.9 (S), 15.3 (R), 47.2 (S)
17.7 (R), 75.2 (S), 87.7 (S)
0.7 (S), 69.8 (S), 77.2 (S)
9.0 (S), 5.3 (S), 30.0 (S)
7.2 (R), 18.4 (S), 29.5 (S)
37.4 (S), 12.9 (R), 3.5 (S)
6.6 (S), 0.8 (R), 11.7 (S)
18.8 (R), 2.1 (R), 5.9 (S)
20.8 (R), 5.7 (S), 6.8 (S)
37.6 (S), 43.1 (R), 2.8 (R)
7.7 (R), 34.8 (R), 4.6 (R)
27.6 (S), 37.4 (R), 8.3 (R)
10.4 (R), 30.3 (R), 7.5 (R)
3.7 (R), 13.2 (R), 4.6 (R)
12.7 (R), 3.9 (R), 2.2 (R)
85.6 (R), 80.4 (S), 70.0 (S)
84.8 (R), 69.3 (S), 62.1 (S)
7
0
2
3
4
5
6
7
8
9
1
35
7
0
2
35
7
0
3
35
7
0
4
35
7
0
5
35
7
0
6
35
7
0
7
35
7
0
Binaphos
35
7
0
5.3, 2.2, 6.5
a
Pressure ) 150 psi (1:1 H2/CO), ligand:Rh ) 1.2:1 for bidentate and 2.2:1 for monodentate phosphites, solvent ) acetone (35 °C runs) and toluene (70
°
C) (3.66 mL), olefins:Rh ) 300:1 at 35 °C and 500:1 at 70 °C. b Percentage conversion of olefins after 3 h. c b/l ) branched-to-linear ratio. Each data point
is an average obtained from two independent runs.
Binaphos (b/l ) 125 vs 7.0 at 35 °C; Table 2, entries 2 and
Use of the Symyx Parallel Pressure Reactor15 (PPR-48)
allowed 48 different catalysts to be screened simultaneously
with styrene, vinyl acetate, and allyl cyanide (144 discrete
reactions). Using this methodology, we have screened a
library of 78 catalysts based on phosphites, phosphines, and
phosphoroamidites. Kelliphite remained the most selective
ligand uncovered by this screen for both allyl cyanide and
vinyl acetate hydroformylation.
9). Enantioselectivities obtained with Binaphos for styrene
and vinyl acetate (Table 2, entry 9) in this study are
9
somewhat lower than reported values. This is most likely
due to different reaction conditions used.
A larger scale reaction in neat vinyl acetate with the Rh-
13
Kelliphite catalyst system proceeded with satisfactory rates
-
1
(
minimum average TOF of 200 h ) and high enantio- and
In summary, we have demonstrated for the first time that
multisubstrate screening in combination with parallel tech-
niques leads to higher reactor throughput. Using this
methodology we have discovered a ligand that gives high
enantio- and regioselectivity for the asymmetric hydroformy-
lation of vinyl acetate. This method should be applicable to
other homogeneous catalyzed reactions.
regioselectivity (82% ee, b/l ) 86).
Ligand 1 was also recently found to lead to quite high
enantio- and regioselectivity in the asymmetric hydroformy-
2
lation of allyl cyanide. Surprisingly, Kelliphite also led to
very high regioselectivity (b/l ) 68.3 at 35 °C) for styrene
hydroformylation; however, the reaction occurred with only
marginal enantioselectivity.
In addition to increased throughput, an additional benefit
of multisubstrate screening in parallel reactors is that relative
reaction rates of different substrates can be measured in one
experiment. The data in Table 2 indicate that allyl cyanide
is the most reactive olefin for all hydroformylation catalysts
in this study. Vinyl acetate is a less reactive substrate and
exhibits lower conversions under these conditions.
Acknowledgment. We thank Drs. Cynthia Rand and Ian
Lennon from Dowpharma for helpful discussions and Mari-
lyn Bokota and Dr. Duane Romer for assistance with PPR-
48 experiments.
14
Supporting Information Available: Experimental pro-
cedures and hydroformylation data for control experiments
using Chiraphite and Kelliphite. This material is available
free of charge via the Internet at http://pubs.acs.org.
We have further increased the throughput of our multi-
substrate screens by utilizing larger arrays of parallel reactors.
OL0487938
(
13) Reaction conditions: VA:Rh ) 2000, neat VA (4 mL), temp ) 60
C, time ) 10 h, 100% conversion.
14) Conversions obtained from experiments with separate olefins (see
(15) (a) Turner, H.; Dales, G.; Vanerden, L.; Van Beek, J. Symyx
Technologies Inc. U.S. Patent 6,306,658, 2001. (b) Tuinstra, H. E.;
Cummins, C. H. AdV. Mater. 2000, 12, 1819. (c) Peil, K. P.; Neithamer, D.
R.; Patrick, D. W.; Wilson, B. E.; Tucker, C. J. Macromol. Rapid Commun.
2004, 25, 119.
°
(
Supporting Information) are very similar to those obtained for the mixture
of olefins.
3280
Org. Lett., Vol. 6, No. 19, 2004