Iron-Catalyzed Hydrogen Production from Formic Acid
A R T I C L E S
15 min and full conversion.14 In 2008, Fukuzumi and co-workers
investigated [Rh(Cp*)(bipy)-(H2O)](SO4) and similar com-
plexes for the hydrogen generation from aqueous formic acid
solutions. They demonstrated that formic acid decomposition
occurs via formate and a hydride complex.15 More recently,
this group demonstrated that heteronuclear iridium-ruthenium
complexes are highly active catalysts for hydrogen generation
Figure 1. Hydrogen generation from biomass via formic acid as an
intermediate compound.
in an aqueous solution under ambient conditions giving a TOF
15b
of ∼426 h-1
.
Himeda et al. focused on iridium complexes
for hydrogen generation from formic acid/sodium formate in
aqueous solution and achieved an initial TOF of 14 000 h-1 at
90 °C.16 Our group and Laurenczy et al. independently
demonstrated that hydrogen generation is also possible under
relatively mild conditions using ruthenium phosphine com-
plexes.17 We identified several ruthenium phosphine complexes
which are capable of generating hydrogen from formic acid
amine adducts selectively at room temperature.18 The catalyst
activity is strongly influenced by the nature and the concentration
of amine in solution, which is not consumed during the reaction
and can easily be recovered from the reaction solution after full
conversion.19 An active catalyst system containing N,N-dim-
ethylhexylamine, [RuCl2(benzene)]2, and 1,2-bis(diphenylphos-
phino)ethane (dppe) was investigated in both batch and con-
tinuous mode and reached at room temperature a turnover
number (TON ) mol of H2/mol of catalyst) of more than
260 000 with a TOF of 900 h-1, which is the highest activity
for hydrogen generation from formic acid.20 Most recently, we
Figure 2. Hydrogen storage via carbon dioxide-formic acid conversion.
Scheme 1. Formic Acid Decomposition Pathways and Their
Thermodynamic Properties9c,10
processing such as fermentation, pyrolysis, and supercritical
reactions and can undergo selective decomposition to hydrogen
and carbon dioxide only in the presence of a catalyst (Figure
1).7 In addition to hydrogen generation, a sustainable and
reversible energy storage cycle can be envisioned by storage
of hydrogen in formic acid and release from it (Figure 2). Here,
carbon dioxide is converted to formic acid or formate derivatives
either electrochemically8 or by catalytic hydrogenation.9 The
resulting products are liquid at ambient conditions and can thus
be handled, stored, and transported easily.
(11) (a) Riena¨cker, G.; Mueller, H. Z. Anorg. Allg. Chem. 1968, 357, 255.
(b) Garcia-Verdugo, E.; Liu, Z.; Ramirez, E.; Garcia-Serna, J.; Fraga-
Dubreuil, J.; Hyde, J. R.; Hamley, P. A.; Poliakoff, M. Green Chem.
2006, 8, 359. (c) Hyde, J. R.; Poliakoff, M. Chem. Commun. 2004,
1482. (d) Hyde, J. R.; Walsh, B.; Singh, J.; Poliakoff, M. Green Chem.
2005, 7, 357. (e) Wiener, H.; Sasson, Y.; Blum, J. J. Mol. Catal. 1986,
35, 277. (f) Zhou, X.; Huang, Y.; Xing, W.; Liu, C.; Liao, J.; Lu, T.
Chem. Commun. 2008, 3540. (g) Ojeda, M.; Iglesia, E. Angew. Chem.,
¨
¨
Int. Ed. 2009, 48, 4800. (h) Kilic¸, E. O; Koparal, A. S.; Ogu¨tveren,
In general, formic acid and formates can be decomposed via
dehydrogenation (eq 1) and dehydration (eq 2) pathways
(Scheme 1). For the subsequent conversion of hydrogen into
electrical energy the latter pathway has to be avoided, because
fuel cells, especially proton exchange membrane fuel cells, do
not tolerate carbon monoxide impurities.
¨
U. B. Fuel Proc. Technol. 2009, 90, 158. (i) Sun, B.; Smirniotis, P. G.
Catal. Today 2003, 88, 49. (j) Kakuta, S.; Toshiyuki, A. Appl. Mater.
Interfaces 2009, 1, 2707.
(12) For an exellent review see: (a) Johnson, C. T.; Morris, D. J.; Wills,
M. Chem. Soc. ReV. 2010, 39, 81. (b) Loges, B.; Boddien, A.; Ga¨rtner,
F.; Junge, H.; Beller, M. Top. Catal. 2010, DOI: 10.1007/s11244-
010-9522-8.
Several heterogeneous11 and homogeneous12,13 catalyst sys-
tems for hydrogen release from HCO2H have been studied since
the beginning of the 20th century, and remarkable results have
been reported in recent years. In 1998, Puddephat et al. studied
the binuclear ruthenium phosphine complex [Ru2(µ-CO)(CO)4(µ-
dppm)2] for selective hydrogen generation from formic acid.
They achieved with their system at room temperature a turnover
frequency (TOF ) mol H2/mol catalyst ·h-1) of ∼500 h-1 after
(13) (a) Coffey, R. S. Chem. Commun. 1967, 18, 923. (b) Forster, D.; Beck,
G. R. Chem. Commun. 1971, 994, 1072. (c) Laine, R. M.; Rinker,
R. G.; Ford, P. C. J. Am. Chem. Soc. 1977, 99, 252. (d) Yoshida, T.;
Ueda, Y.; Otsuka, S. J. Am. Chem. Soc. 1978, 100, 3941. (e) Strauss,
S. H.; Whitmire, K. H.; Shriver, D. F. J. Organomet. Chem. 1979,
174, C59. (f) Paonessa, R. S.; Trogler, W. C. J. Am. Chem. Soc. 1982,
104, 3529. (g) King, R. B.; Bhattacharyya, N. K. Inorg. Chim. Acta
1995, 237, 65. (h) Man, M. L.; Zhou, Z.; Ng, S. M.; Lau, C. P. Dalton
Trans. 2003, 3727.
(14) (a) Gao, Y.; Kuncheria, J.; Yap, G. P. A.; Puddephatt, R. J. Chem.
Commun. 1998, 2365. (b) Gao, Y.; Kuncheria, J. K.; Jenkins, H. A.;
Puddephatt, R. J.; Yap, G. P. A. J. Chem. Soc., Dalton Trans. 2000,
3212. (c) Shin, J. H.; Churchill, D. G.; Parkin, G. J. Organomet. Chem.
2002, 642, 9.
(7) (a) Reunanen, J.; Oinas, P.; Nissinen, T. A process for recovery of
formic acid. PCT Int. Appl., 2009. (b) Kruse, A.; Gawlik, A. Ind.
Eng. Chem. Res. 2003, 42, 267. (c) Hayes, D. J.; Fitzpatrick, S.; Hayes,
M. H. B.; Ross, J. R. H. in Biorefineries-Industrial Processes and
Products; Kamm, B.; Gruber, P. R., Kamm, M., Ed.; Wiley-VCH,
Weinheim, 2006; p 139.
(8) (a) Benson, E. E.; Kubiak, C. P.; Sathrum, A. J.; Smieja, J. M. Chem.
Soc. ReV. 2009, 38, 89. (b) Marks, J. T. et al. Chem. ReV. 2001, 101,
953.
(15) (a) Fukuzumi, S.; Kobayashi, T.; Suenobu, T. ChemSusChem 2008,
1, 827. (b) Fukuzumi, S.; Kobayashi, T.; Suenobu, T. J. Am. Chem.
Soc. 2010, 132, 1496.
(16) Himeda, Y. Green Chem. 2009, 11, 2018.
(17) (a) Fellay, C.; Yan, N.; Dyson, P. J.; Laurenczy, G. Chem.sEur. J.
2009, 15, 3752. (b) Gan, W.; Dyson, P. J.; Laurenczy, G. React. Kinet.
Catal. Lett. 2009, 89, 205. (c) Loges, B.; Boddien, A.; Junge, H.;
Beller, M. Angew. Chem., Int. Ed. 2008, 47, 3962. (d) Fellay, C.;
Dyson, P. J.; Laurenczy, G. Angew. Chem., Int. Ed. 2008, 47, 3966.
(18) Boddien, A.; Loges, B.; Junge, H.; Beller, M. ChemSusChem 2008,
1, 751.
(9) (a) Leitner, W. Angew. Chem., Int. Ed. Engl. 1995, 34, 2207. (b) Jessop,
P. G.; Joo´, F.; Tai, C. C. Coord. Chem. ReV. 2004, 248, 2425. (c)
Jessop, P. G. in The Handbook of Homogeneous Hydrogenation; de
Vries, J. G., Elsevier, C. J., Eds.; Wiley-VCH: Weinheim, 2007; p
489.
2009).
(19) Junge, H.; Boddien, A.; Capitta, F.; Loges, B.; Noyes, J. R.; Gladiali,
S.; Beller, M. Tetrahedron Lett. 2009, 50, 1603.
(20) Boddien, A.; Loges, B.; Junge, H.; Ga¨rtner, F.; Noyes, J. R.; Beller,
M. AdV. Synth. Catal. 2009, 351, 2517.
9
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