C O M M U N I C A T I O N S
turnoVer frequencies greater than ca. 3000 h-1 oVer 90% consump-
tion of the substrate.
the CdC double bond occurs at the same enantioface for all
substrates. A useful quadrant diagram, based on the assumption of
a trigonal bipyramidal coordination environment with diequatorial
phosphorus atoms, for rationalizing the product stereochemistry is
shown. We emphasize that this model is purely mnemonic. Better
characterization of catalyst coordination geometries through spec-
troscopic and computational model studies is underway.
Both the high cost of rhodium catalysts and the attractiveness
of applying hydroformylation to more substituted alkenes emphasize
the importance of hydroformylation activity. Our reaction screening
conditions lead to higher catalyst activities than commonly are
reported, particularly, with bis-3,4-diazaphospholane ligands. For
example, in the presence of 1.2 equiv of 7a at a total substrate:Rh
loading of 30 000:1 under 500 psig of syn gas at 80 °C, conversions
of styrene, allyl cyanide, and vinyl acetate are 85, 100, and 86% in
just 3 h. Analysis of gas uptake curves under these conditions
reveals average turnover frequencies of at least ca. 9000 h-1, or
2.5 turnovers s-1, over 90% conversion of substrate. Under
otherwise identical conditions, hydroformylations with bis-3,4-
diazaphospholane-modified catalysts proceed approximately twice
as fast as bisphosphites 11 and 13 and the mixed phosphine-
phosphite 10.
Interestingly, hydroformylation rate laws with bis-3,4-diaza-
phospholanes are approximately first-order in alkene and indepen-
dent of the synthesis gas pressure in the range of 100-500 psi.
Preliminary data suggest that the rate law for hydroformylation is
zero-order in both H2 and CO concentrations over the 60-80 °C
temperature range. Furthermore, the data indicate that styrene
enantioselectivities and regioselectivities primarily respond to
changes in CO pressure; lower CO partial pressure results in lower
selectivity. Allyl cyanide selectivities also decrease with decreased
CO pressure, but the effect is not so large. These rate laws are
consistent with bimolecular reaction of the catalyst and substrate
comprising or preceding the turnover-limiting step. Presumably,
the influence of CO pressure on hydroformylation selectivity for
styrene (both enantiomeric excess and b:l ratio), combined with
the absence of any influence of gas pressures on the rate of styrene
conversion, reflects the interruption of Rh-alkyl isomerizations
occurring after the turnover-limiting step. More detailed examination
of the reaction kinetics is underway.
In summary, bis-3,4-diazaphospholanes bearing benzoic acid in
the 2 and 5 positions are readily accessible and extensible ligands
for enantioselective hydroformylation with rhodium catalysts.
Significantly, these ligands demonstrate effective control of regio-
and enantioselectivity for three different classes of substrates while
achieving very high catalyst activity. These properties suggest broad
applicability to catalytic, enantioselective synthesis of aldehydes.
Acknowledgment. We thank Dowpharma for financial support
of this research. We thank Mr. Ryan Nelson for numerous
contributions.
Supporting Information Available: Experimental procedures and
spectral data for all new compounds. Crystallographic data for 7a,
including a CIF file. This material is available free of charge via the
References
(1) Claver, C.; van Leeuwen, P. W. N. M. In Rhodium Catalyzed Hydro-
formylation; Claver, C., van Leeuwen, P. W. N. M., Eds.; Kluwer
Academic Publishers: Dordrecht, The Netherlands, 2000.
(2) Landis, C. R.; Jin, W.; Owen, J. S.; Clark, T. P. Angew. Chem., Int. Ed.
2001, 40, 3432-3434.
(3) Clark, T. P.; Landis, C. R. J. Am. Chem. Soc. 2003, 125, 11792-11793.
(4) Landis, C. R.; Clark, T. P. Proc. Natl. Acad. Sci. U.S.A. 2004, 101, 5428-
5432.
(5) Nozaki, K.; Sakai, N.; Nanno, T.; Higashijima, T.; Mano, S.; Horiuchi,
T.; Takaya, H. J. Am. Chem. Soc. 1997, 119, 4413-4423.
(6) Cobley, C. J.; Gardner, K.; Klosin, J.; Praquin, C.; Hill, C.; Whiteker, G.
T.; Zanotti-Gerosa, A.; Petersen, J. L.; Abboud, K. A. J. Org. Chem. 2004,
69, 4031-4040.
(7) Cobley, C. J.; Klosin, J.; Qin, C.; Whiteker, G. Org. Lett. 2004, 6, 3277-
3280.
Hydroformylation of vinyl acetate, allyl cyanide, or styrene in
the absence of the other substrates yields selectivities and rates
identical to those of the mixed substrates. Single substrate hydro-
formylations using ligand 7a at 80 °C and 150 psig syn gas with
1.8 × 10-4 M Rh achieve 50% conversion of 10 000 equiv of
substrate in 30 (allyl cyanide), 37 (vinyl acetate), and 60 min
(styrene). These data demonstrate, at least for these substrates and
catalysts, that the mixed substrate screening protocol does not
introduce kinetic or selectivity artifacts. Without appropriate
controls, one cannot assume that mixed substrate and single
substrate results, particularly with respect to apparent rates, will
be identical.
(8) Breeden, S.; Cole-Hamilton, D. J.; Foster, D. F.; Schwarz, G. J.; Wills,
M. Angew. Chem., Int. Ed. 2000, 39, 4106-4108.
(9) (a) Babin J. E.; Whiteker, G. T. Patent WO 93/03830, 1992. (b) Whiteker,
G. T.; Briggs, J. R.; Babin, J. E.; Barner, B. A. In Catalysis of Organic
Reactions; Morrell, D. G., Ed.; Marcel Dekker: New York, 2003; p 359.
(10) Dieguez, M.; Pamies, O.; Ruiz, A.; Castillon, S.; Claver, C. Chem.sEur.
J. 2001, 7, 3086-3094.
The absolute configurations of the branched hydroformylation
products for styrene (R), allyl cyanide (R), and vinyl acetate (S)
with ligand 7a reveal that formal addition of formaldehyde across
(11) Tang, W.; Zhang, X. Chem. ReV. 2003, 103, 3029-3070.
JA050148O
9
5042 J. AM. CHEM. SOC. VOL. 127, NO. 14, 2005