C O M M U N I C A T I O N S
Scheme 1. Catalytic Cycle for Dehydrogenation of AB with the Ru Catalyst in THF and Gas Phase from DFT Calculationsa16
a Black and blue lines indicate different conformers of the P,N ligands of the Ru species. Reported values are in kcal/mol.
Scheme 2. Reduction of Ketones and Imines Using PyrAB as the
Source of H2
References
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tion precatalysts).21 AB dehydrogenation at 8 to form dihydride 9
is slightly endothermic; however, a reaction coordinate scan in
forward and reverse directions revealed that this step does not have
a kinetic barrier in gas phase calculations. The largest kinetic barrier
from these calculations involves the formation of dihydrogen
complex 11 via transition state 10 that can subsequently dissociate
H2 to regenerate catalyst 7. The intermediacy of a species similar
to dihydride 9 is further supported through the successful coupling
of AB dehydrogenation with CdO, CdN hydrogenation (Vide infra)
since Ru-dihydrides are known to mediate H2 delivery to these
functional groups.
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We have also determined that AB-ketone/imine transfer hydro-
genation may be achieved.22 Superior outcomes are observed with
precatalyst 3, which is less reactive than 1 in hydrogen release
processes. Use of pyrrolidine borane (PyrAB) in conjunction with
1.5 mol% precatalyst 3 and 3 mol% KOtBu efficiently induces the
hydrogenation of several organic substrates (Scheme 2).16 In each
instance, no detectable background reduction was observed in the
absence of Ru catalyst over the same reaction time.
(14) Control reactions run with AB and 10 mol % KOtBu in the absence of
catalyst eliminated the possibility of base-enabled dehydrogenation.
(15) Staubitz, A.; Presa Soto, A.; Manners, I. Angew. Chem., Int. Ed. 2008, 47,
Early View.
(16) See Supporting Information for experimental and computational details.
(17) 1H, 13C, and 11B NMR revealed the presence of a complex reaction mixture.
See Supporting Information.
Significant challenges remain in the development of chemical
hydrogen storage. The full potential of AB will only be attained
by increasing the amount of H2 released to well over 1.0 equiv
and by solving the important problem of regenerating AB from
the waste products;23 however, the exceptionally low catalyst
loadings, mild reaction conditions, rapid release of H2, and high
concentration achievable by this system represent a new opportunity
for approaching hydrogen storage/release goals.24
(18) Lane, C. F. U. S. DOE Hydrogen Program; 2007 Annual Progress Report,
Section IV.B.5j, 2007.
(19) Homogenous catalysis was confirmed, as the addition of mercury to the
reaction medium had no effect on H2 evolution.
(20) (a) Noyori, R.; Yamakawa, M.; Hashiguchi, S. J. Org. Chem. 2001, 66,
7931. (b) Sandoval, C. A.; Ohkuma, T.; Mun˜iz, K.; Noyori, R. J. Am. Chem.
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Noyori, R. Angew, Chem, Int. Ed. Engl. 1997, 36, 285.
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(b) Ohkuma, T.; Koizumi, M.; Mun˜iz, K.; Hilt, G.; Kabuto, C.; Noyori, R.
J. Am. Chem. Soc. 2002, 124, 6508.
(22) For uncatalyzed reductions using amine-boranes, see: (a) Uyeda, C.; Biscoe,
M.; LePlae, P.; Breslow, R. Tetrahedron Lett. 2006, 47, 127. (b) Allwood,
B. L.; Shahriari-Zavareh, H.; Stoddart, J. F.; Williams, D. J. Chem.
Commun. 1984, 22, 1461 For the catalyzed transfer hydrogenation of
alkenes, see: (c) Clark, T. J.; Lee, K.; Manners, I. Chem.sEur. J. 2006,
12, 8634. (d) Jiang, Y.; Berke, H. Chem. Commun. 2007, 3571.
(23) For theoretical studies on the properties of AB and its decomposition
products, see: Caetano, M. R.; Gerbrand, C. J. Chem. Phys. 2007, 126,
184703. For studies on regeneration of AB: (b) Hausdorf, S.; Baitalow, F.;
Wolf, G.; Mertens, F. O. R. L. Int. J. Hydr. Energy 2008, 33, 608. (c)
Sneddon, L. G. U.S. DOE Hydrogen Program; 2007 Annual Progress
Report,Section IV.B.5e, 2007.
Acknowledgment. NSERC, the University of Ottawa, and the
Research Corporation are thanked for financial support. Kanata
Chemical Technologies (Dr. K. Abdur-Rashid) is thanked for the
donation of catalysts. Drs. A. A. Mommers, C. W. Kazakoff, and
P. M. Mayer are thanked for mass spectrometry assistance, and
Prof. T. K. Woo is thanked for use of computing facilities funded
by the CFI. We thank Prof. R. Tom Baker for helpful discussions.
Supporting Information Available: Experimental procedures,
additional information, computational details, and DFT structures.
This material is available free of charge via the Internet at http://
pubs.acs.org.
(24) Just prior to the submission of this manuscript we became aware of similar
work being performed independently at Kanata Chemical Technologies (Dr.
Abdur-Rashid) using similar catalysts.
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