C O M M U N I C A T I O N S
Figure 5. Rhodium (5 wt %-Rh/Al2O3, 1.0 mol %-Rh) catalyzed H2 release
from a 22.7-wt % aqueous solution of ammonia triborane (1.8 mmol)
yielding 6.1 wt % H2 [wt % ) H2-wt/(NH3B3H7 + H2O + Rh/Al2O3-wts)].
Figure 3. Hydrogen evolution following repeated additions of ammonia
triborane to an aqueous solution containing 5 wt %-Rh/Al2O3.
system. Under these concentrated conditions, 11B NMR studies show
that the hydrolysis reaction yields condensed polyborates, which
-
10
3 4
upon addition of water form mixtures of B(OH) /B(OH) . Thus,
the real utility of this process as a chemical hydrogen storage system
will ultimately depend on the development of new “off-board”
methods to regenerate ammonia triborane from these borates.
Acknowledgment. We thank the U.S. Department of Energy
Center of Excellence for Chemical Hydrogen Storage for support.
We also thank Dr. Goji Kodama for his helpful comments.
Figure 4. Hydrogen release at different temperatures (1, 50; 2, 35; b,
Supporting Information Available: Experimental procedures for
the synthesis of NH B H and the hydrogen release studies. This
3 3 7
material is available free of charge via the Internet at http://pubs.acs.org.
2
0; 9, 0 °C) versus time for 4.9 wt % aqueous solutions of ammonia
triborane catalyzed by 5 wt %-Rh/Al2O3 (1.1 mol %-Rh).
2 3
both the [Rh(COD)(µ-Cl)] and RhCl appear to undergo reduction
References
upon ammonia triborane addition suggesting that Rh clusters and/
or colloids may be the active catalytic species in these systems.6
The rhodium catalysts have also been found to have extended
lifetimes. Thus, as indicated in Figure 3, hydrogen evolution
measurements following periodic additions of ∼9 mg (∼0.16 mol)
of solid ammonia triborane to a 2 mL aqueous borate-buffered (pH
maintained between 7.2 and 8.0) solution containing 1.3 mg (0.012
(
1) (a) Amendola, S. C.; Sharp-Goldman, S. L.; Janjua, M. S.; Kelly, M. T.;
Petillo, P. J.; Binder, M. J. Power Sources 2000, 85, 186-189. (b)
Amendola, S. C.; Sharp-Goldman, S. L.; Janjua, M. S.; Spencer, N. C.;
Kelly, M. T.; Petillo, P. J.; Binder, M. Int. J. Hydrogen Energy 2000, 25,
969-975. (c) Dong, H.; Yang, H.; Ai, X.; Cha, C. Int. J. Hydrogen Energy
2
003, 28, 1095-1100. (d) Jeong, S. U.; Kim, R. K.; Cho, E. A.; Kim,
H.-J.; Nam, S.-W.; Oh, I.-H.; Hong, S.-A.; Kim, S. H. J. Power Sources
2
005, 144, 129-134. (e) Krishnan, P.; Yang, T.-H.; Lee, W.-Y.; Kim,
C.-S. J. Power Sources 2005, 143, 17-23. (f) Kojima, Y.; Suzuki, K.;
Fukumoto, K.; Sasaki, M.; Yamamoto, T.; Kawai, Y.; Hayashi, H. Int. J.
Hydrogen Energy 2002, 27, 1029-1034.
mmol Rh) of 5 wt %-Rh/Al
release rates over 10 cycles.
An Arrhenius plot of the initial rate data (Figure 4) for hydrogen
release from a 5 wt %-Rh/Al (1.1 mol %-Rh) catalyzed reaction
2 3
O showed little change in the hydrogen
(2) (a) Chandra, M.; Xu, Q. J. Power Sources 2006, 156, 190-194.
(
b) Chandra, M.; Xu, Q. J. Power Sources 2006, 159, 855-860. (c) Kelly,
H. C.; Marriott, V. B. Inorg. Chem. 1979, 18, 2875-2878. (d) T-Raissi,
A. Proc. 2002 U.S. DOE Hydrogen Program ReV. 2002, 10;
www1.eere.energy.gov/hydrogenandfuelcells/pdfs/32405b15.pdf.
2 3
O
of a 4.9 wt % ammonia triborane solution at different temperatures
yielded an activation energy of 13.4 kcal/mol, which is in the range
(3) (a) Kodama, G.; Parry, R. W.; Carter, J. C. J. Am. Chem. Soc. 1959, 81,
3534-3538. (b) Nordman, C. E.; Reimann, C. J. Am. Chem. Soc. 1959,
81, 3538-3543.
found for metal-catalyzed NaBH
depending on the catalyst ).
4
hydrolysis (∼9 to 18 kcal/mol,
(4) Brellochs, B.; Binder, H. Angew. Chem., Int. Ed. Engl. 1988, 27, 262-
1
263.
(5) (a) Nainan, K. C.; Ryschkewitsch, G. E. Inorg. Nucl. Chem. Lett. 1970,
Calculations of the standard heats of eqs 1-3 using standard
6
, 765-766. (b) Ryschkewitsch, G. E.; Nainan, K. C. Inorg. Synth. 1974,
enthalpies of formation,7 indicate that hydrogen release from
15, 113-114.
(6) (a) Chen, Y.; Fulton, J. L.; Linehan, J. C.; Autrey, T. J. Am. Chem. Soc.
3
NH B
H
3 7
is slightly more exothermic (15.8 kcal/mol-H
2
) than that
2005, 127, 3254-3255. (b) Chen, Y.; Fulton, J.; Linehan, J.; Autrey, T.
from either NaBH
4
(14.9 kcal/mol-H ) or NH BH (12.7 kcal/mol-
2 3 3
Prepr. Symp.sAm. Chem. Soc., DiV. Fuel Chem. 2004, 49, 972-973. (c)
Schulz, J.; Roucoux, A.; Patin, H. Chem. Commun. 1999, 535-536.
7) (a) CRC Handbook of Chemistry and Physics, 85th ed.; CRC Press: New
York, 2004-2005. (b) A value of -49 kcal/mol for the standard heat of
formation of ammonia triborane was taken from Dunn Engineering,
2
H ), but is much less than the hydrolytic reactions of metal hydrides
(
8
(
e.g., LiAlH
4
, ∼30 kcal/mol-H
2
).
As illustrated in Figure 5, the hydrolysis reaction of a 22.7 wt
“
Rocket Engine Specific Impulse Program” http://www.dunnspace.com/
isp.htm (page 8) (accessed June 2006).
(8) (a) Messer, C. E.; Fasolino, L. G.; Thalmayer, C. E. J. Am. Chem. Soc.
%
sample of aqueous ammonia triborane containing 0.30 g of H
(1.8 mmol), and 0.04 g of 5 wt %-Rh/Al
0.02 mmol of Rh) produced 0.027 g (13.5 mmol, 7.5 equiv) of H
2
O,
0.10 g of NH
3
B
H
3 7
O
2 3
1
955, 77, 4524-4526. (b) Davis, W. D.; Mason, L. S.; Stegeman, G. J.
(
(
2
Am. Chem. Soc. 1949, 71, 2775-2781.
measured by gas buret) over 3 h at 21 °C. This result corresponds
based on materials [wt % ) H
-wts)] and suggests that the DOE
007 total-system target of 4.5 wt % for hydrogen release from a
chemical hydrogen storage system might be attainable with this
(9) U.S. DOE, “Hydrogen, Fuel Cells & Infrastructure Technologies Program”,
http://www.eere.energy.gov/hydrogenandfuelcells/storage/pdfs/ (accessed
June 2006).
(10) (a) Momii, R. K.; Nachtrieb, N. H. Inorg. Chem. 1967, 6, 1189-1192.
to a production of 6.1 wt % H
wt/(NH + H O + Rh/Al
2
2
2
-
B H
3 3 7
2
O
2 3
9
(b) Smith, H. D., Jr.; Wiersema, R. J. Inorg. Chem. 1972, 11, 1152-1154.
JA064526G
J. AM. CHEM. SOC.
9
VOL. 128, NO. 43, 2006 13993