RESEARCH
| REPORTS
6. T. Hashimoto, in Asymmetric Organocatalysis 2: Brønsted
Base and Acid Catalysts, and Additional Topics, K. Maruoka, Ed.
(Georg Thieme Verlag, Stuttgart, New York, 2012),
pp. 279–296.
CATALYSIS
7. T. Akiyama, J. Itoh, K. Yokota, K. Fuchibe, Angew. Chem. Int. Ed.
43, 1566–1568 (2004).
8. D. Uraguchi, M. Terada, J. Am. Chem. Soc. 126, 5356–5357
(2004).
9. I. Ahmed, D. A. Clark, Org. Lett. 16, 4332–4335 (2014).
10. D. Kampen, C. M. Reisinger, B. List, Top. Curr. Chem. 291,
395–456 (2010).
11. T. James, M. van Gemmeren, B. List, Chem. Rev. 115,
9388–9409 (2015).
12. T. Akiyama, Chem. Rev. 107, 5744–5758 (2007).
13. T. Akiyama, K. Mori, Chem. Rev. 115, 9277–9306 (2015).
14. A. Berkessel, P. Christ, N. Leconte, J.-M. Neudörfl, M. Schäfer,
Eur. J. Org. Chem. 2010, 5165–5170 (2010).
15. D. Nakashima, H. Yamamoto, J. Am. Chem. Soc. 128,
9626–9627 (2006).
16. M. Treskow, J. Neudörfl, R. Giemoth, Eur. J. Org. Chem. 2009,
3693–3697 (2009).
17. G. B. Rowland et al., J. Am. Chem. Soc. 127, 15696–15697
(2005).
Palladium-tin catalysts for the direct
synthesis of H2O2 with high selectivity
Simon J. Freakley,1*† Qian He,2,3† Jonathan H. Harrhy,1 Li Lu,2 David A. Crole,1
David J. Morgan,1 Edwin N. Ntainjua,1 Jennifer K. Edwards,1 Albert F. Carley,1
Albina Y. Borisevich,3,4 Christopher J. Kiely,2 Graham J. Hutchings1*
The direct synthesis of hydrogen peroxide (H2O2) from H2 and O2 represents a potentially
atom-efficient alternative to the current industrial indirect process. We show that the
addition of tin to palladium catalysts coupled with an appropriate heat treatment cycle
switches off the sequential hydrogenation and decomposition reactions, enabling
selectivities of >95% toward H2O2. This effect arises from a tin oxide surface layer that
encapsulates small Pd-rich particles while leaving larger Pd-Sn alloy particles exposed.
We show that this effect is a general feature for oxide-supported Pd catalysts containing an
appropriate second metal oxide component, and we set out the design principles for producing
high-selectivity Pd-based catalysts for direct H2O2 production that do not contain gold.
18. F. Xu et al., J. Org. Chem. 75, 8677–8680 (2010).
19. H. Yanai, T. Taguchi, J. Fluor. Chem. 174, 108–119 (2015).
20. H. Yamamoto, D. Nakashima, in Acid Catalysis in Modern
Organic Synthesis, vol. 1, H. Yamamoto, K. Ishihara, Eds.
(Wiley-VCH, Weinheim, 2008), pp. 35–62.
21. F. G. Bordwell, G. E. Drucker, H. E. Fried, J. Org. Chem. 46,
632–635 (1981).
22. M. I. Bruce, A. H. White, Aust. J. Chem. 43, 949–995
(1990).
23. O. Diels, Ber. Dtsch. Chem. Ges. 75, 1452–1467 (1942).
24. O. Diels, U. Kock, Liebigs Ann. Chem. 556, 38–50 (1944).
25. I. E. Mikhailov, G. A. Dushenko, V. I. Minkin, L. P. Olekhnovich,
J. Org. Chem. USSR 20, 1509–1514 (1984).
26. E. Le Goff, R. LaCount, J. Org. Chem. 29, 423–427 (1964).
27. K. Kaupmees, N. Tolstoluzhsky, S. Raja, M. Rueping, I. Leito,
Angew. Chem. Int. Ed. 52, 11569–11572 (2013).
28. S. E. Reisman, A. G. Doyle, E. N. Jacobsen, J. Am. Chem. Soc.
130, 7198–7199 (2008).
29. N. Z. Burns, M. R. Witten, E. N. Jacobsen, J. Am. Chem. Soc.
133, 14578–14581 (2011).
30. M. R. Witten, E. N. Jacobsen, Angew. Chem. Int. Ed. 53,
5912–5916 (2014).
31. G. C. Tsui, L. Liu, B. List, Angew. Chem. Int. Ed. 54, 7703–7706
(2015).
32. J. H. Kim, I. Čorić, S. Vellalath, B. List, Angew. Chem. Int. Ed.
52, 4474–4477 (2013).
33. I. Čorić, B. List, Nature 483, 315–319 (2012).
34. A. Borokiva, P.-I. Tang, S. Klapman, P. Nagorny, Angew. Chem.
Int. Ed. 52, 13424–13428 (2013).
35. L. Ratjen, P. García-García, F. Lay, M. E. Beck, B. List,
Angew. Chem. Int. Ed. 50, 754–758 (2011).
36. G. L. Hamilton, E. J. Kang, M. Mba, F. D. Toste, Science 317,
496–499 (2007).
37. K. Brak, E. N. Jacobsen, Angew. Chem. Int. Ed. 52, 534–561
(2013).
38. M. Mahlau, B. List, Angew. Chem. Int. Ed. 52, 518–533 (2013).
urrently, the demand for H2O2 is met by
an indirect process, which produces H2O2
through the sequential hydrogenation and
oxidation of a substituted anthraquinone
(1). For economic reasons, the process is
Although this approach was very successful on an
activated carbon support material, the same block-
ing effect could not be fully achieved on other com-
mercial support materials such as SiO2 and TiO2.
Because O2 dissociation is undesirable in the
direct synthesis of H2O2, the reaction can be
treated as a selective hydrogenation of O2. We
explored other Pd-metal combinations that are
used for selective hydrogenation reactions as po-
tential catalysts for H2O2 synthesis, focusing on
nonprecious metals to lower costs. Tin (Sn) has
been used to modify hydrogenation catalysts in
reactions such as the selective hydrogenation of
1,3-butadiene (11). Further examples have been
reported for the liquid-phase hydrogenation of
hexa-1,3-diene and hexa-1,5-diene (12) as well as
the hydrogenation of unsaturated alcohols (13).
The addition of Sn to Pd or Pt can alter the behav-
ior of the catalyst during hydrogenation reactions
and, in particular, may have an effect on subse-
quent reactions of the products with the catalyst.
We report the development of Sn-containing
Pd catalysts on commercially available TiO2 and
SiO2 supports that can achieve >95% selectivity
toward direct H2O2 synthesis. These catalysts,
after being subjected to an appropriate heat
treatment regimen, obviate the need for pre-
treating the support with acids and contain far
less precious metal than Au-Pd catalysts. We
also present the general principles whereby
high-selectivity catalysts can be obtained with
other Pd-metal combinations.
C
operated at large scale and produces concen-
trated H2O2. In reality, many applications, such
as disinfection and water purification, require
only dilute H2O2, which means that concen-
trated H2O2 must be diluted at the point of use.
Research into the direct synthesis of H2O2 from
H2 and O2 as a more suitable solution to small-
scale, on-site H2O2 production has focused on
palladium (Pd)–based catalysts (2–4). However,
H2O2 is itself highly reactive, and the presence
of H2 favors hydrogenation and decomposition
reactions that form water. The addition of strong
acids and halides to the reaction medium can
suppress the sequential hydrogenation and deg-
radation in supported Pd catalysts (5) but can
also promote metal leaching and requires further
purification of the H2O2 before use.
Bimetallic Au-Pd alloy catalysts have been ex-
tensively studied as catalysts for the direct H2O2
synthesis reaction on a number of support mate-
rials, including TiO2, SiO2, and activated carbon
(6–9). Yields comparable to monometallic Pd cat-
alysts can be achieved without the need for acid
and halide additives in the reaction mixture, and
95% selectivity to H2O2 can be achieved with Au-
Pd alloy nanoparticles (NPs) dispersed on an acid-
pretreated activated carbon support material (10).
Hydrogen peroxide hydrogenation could be de-
coupled from H2O2 synthesis with an acid pre-
treatment that blocked sites on the carbon support
material responsible for H2O2 degradation (10).
ACKNOWLEDGMENTS
Funding for this work was provided by the National Science
Foundation under CHE-0953259. C.D.G. is grateful for a
National Science Foundation Graduate Fellowship. We thank
P. Quinlivan and the Parkin group, as well as D. Paley, for x-ray
structure determination and the National Science Foundation
(CHE-0619638) for acquisition of an x-ray diffractometer.
We are grateful to M. Vetticatt (State University of New York,
Binghamton) and V. Roytman for assistance with the
stereochemical models. Metrical parameters for the structures
of 7•NMe4 and the oxocarbenium Aldol product are available
free of charge from the Cambridge Crystallographic Data Centre
under CCDC 1450055 and 1450056, respectively.
Simple impregnation of Au and Pd metal salts
onto many catalyst supports has been shown to
generate highly active catalysts for direct H2O2
synthesis. In addition, high-temperature calcina-
tion or reduction treatments are known to be
crucial to improve the stability of the catalyst. As
a starting point, we used this simple catalyst
preparation methodology to prepare a 2.5 weight
percent (wt%) Pd–2.5 wt % Sn/TiO2 catalyst as
well as its monometallic analogs (8, 10). A syn-
ergistic effect toward higher H2O2 productivity
was observed when both metals were present
1Cardiff Catalysis Institute and School of Chemistry, Cardiff
University, Cardiff CF10 3AT, UK. 2Department of Materials
Science and Engineering, Lehigh University, Bethlehem, PA
18015, USA. 3Materials Science and Technology Division, Oak
Ridge National Laboratory, Oak Ridge, TN 37831, USA. 4Center
for Nanophase Materials Sciences, Oak Ridge National
Laboratory, Oak Ridge, TN 37831, USA.
SUPPLEMENTARY MATERIALS
Materials and Methods
Figs. S1 to S4
Tables S1 to S4
References (39–57)
20 July 2015; accepted 27 January 2016
10.1126/science.aad0591
*Corresponding author. E-mail: hutch@cf.ac.uk (G.J.H.); freakleys@
cf.ac.uk (S.J.F.) †These authors contributed equally to this work.
SCIENCE sciencemag.org
26 FEBRUARY 2016 • VOL 351 ISSUE 6276 965