Catalytic hydrogenation of cyclohexene
Platinum-catalyzed hydrogenation.
Acknowledgements
A
reactor containing
This work was financially supported by the research projects CNR-
INSTM PROMO, FIRB-MIUR RBNE033KMA “Molecular
compounds and hybrid nanostructured materials with resonant
and non-resonant optical properties for photonic devices”, FISR-
MIUR “Inorganic hybrid nanosystems for the development and
the innovation of fuel cells”, CARIPARO 2006 “Multi-layer
optical devices based on inorganic and hybrid materials by
innovative synthetic strategies” and by Ministero dell’Universita
e della Ricerca Universitaria (MIUR), 2004–6. Thanks are due to:
Chimet, S.pA., Badia al Pino, Arezzo, Italy, for loans of platinum
and palladium, and for the analyses of the metal content in most
2
5 mL of cyclohexane saturated with dihydrogen and a flame-
sealed thin-walled glass ampoule containing the platinum-loaded
-
3
silica (0.143 g, 5.6 ¥ 10 mmol of platinum) was connected to
a gas-volumetric apparatus under a dihydrogen atmosphere. By
◦
operating at 24.9 C, 0.7 mL of a 1.69 M solution of cyclohexene
in cyclohexane were introduced (1.18 mmol, corresponding to
a cyclohexene/Pt molar ratio of 211). When the ampoule was
`
broken, the absorption of H
2
started. It was recorded as a function
of time and found to be substantially linear, corresponding to 14.8
-
1
-1
(
(
mmol of H
absorbed H
2
) ¥ min ¥ mmolPt . The plot of the molar ratio
)/Pt vs. time of a typical experiment is in Fig. 7.
2
of the silica-supported systems; Prof. E. Tondello, Universita di
Padova, for his interest and encouragement; Prof. P. Colombo and
Prof. A. Martucci, Universit a` di Padova, for XRD measurements
and helpful discussions.
`
Palladium-catalyzed hydrogenation.
A reactor containing
2
0 mL of cyclohexane saturated with dihydrogen and a flame-
sealed thin-walled glass ampoule containing the palladium-loaded
-
3
silica (0.134 g, 9.6 ¥ 10 mmol of metal) was connected with
a gas-volumetric apparatus under a dihydrogen atmosphere. By
References
◦
operating at 24.9 C, 0.7 mL of a solution of cyclohexene in
1
(a) P. K. Jain, X. Huang, I. H. El-Sayed and E. M. El-Sayed, Acc. Chem.
Res., 2008, 41, 1578; (b) I. Favier, S. Massou, E. Teuma, K. Philippot,
B. Chaudret and M. G o´ mez, Chem. Commun., 2008, 3296; (c) G. A.
Samorjai, F. Tao and J. Y. Park, Top. Catal., 2008, 47, 1; (d) R. W.
Murray, Chem. Rev., 2008, 108, 2688; (e) D. Astruc, Transition-metal
Nanoparticles in Catalysis: From Historical Background to the State-
of-the Art in Nanoparticles and Catalysis,ed. D. Astruc, Wiley-VCH
Verlag, Weinheim, 2008, pp. 1–48; (f) H. B o¨ nnemann and K. S.
Nagabhushana, Metal Nanoclusters: synthesis and strategies for their
size control in Metal Nanoclusters in Catalysis and Materials Science,
The Issue of Size Control, ed. B. Corain, G. Schmid and N. Toshima,
Elsevier B. V., Amsterdam, 2008, pp. 21–48.
cyclohexane (1.69 M, 1.18 mmol) were introduced, corresponding
to a cyclohexene/Pd molar ratio of 123. After breakage of the
ampoule, the absorption of H
2
vs. time was measured and found
to be substantially linear and corresponding to 5.6 (mmol of H
2
)
1
-1
¥
min- ¥ mmolPd . The plot of the molar ratio (absorbed H
)/Pd
2
vs. time is in Fig. 8.
Conclusion
2
3
D Poondi and M. A. Vannice, J. Catal., 1996, 161, 742.
For palladium–catalyzed hydrogenations, see: (a) Y. Gao, C.-A. Chen,
H.-M. Gau, J. A. Bailey, E. Akhadov, D. Williams and H.-L. Wang,
Chem. Mater., 2008, 20, 2839; (b) A. M. Doyle, S. K. Shaikhutdinov and
H.-J. Freund, Angew. Chem., Int. Ed., 2005, 44, 629; (c) For platinum-
catalyzed hydrogenations, see: F. O. Ernst, R. B u¨ chel, R. Strobel and
S. E. Pratsinis, Chem. Mater., 2008, 20, 2117; (d) T. Onoe, S. Iwamoto
and M. Inoue, Catal. Commun., 2007, 8, 701.
Our approach to the preparation of the palladium- or platinum-
containing catalysts was based on an attempt to minimize the
intrinsic differences between the two metals in the process of
loading on the inorganic matrix. As the metal particles were
prepared by a substantially identical process at room temperature,
starting from molecular precursors of the same type, we are con-
fident that our goal was accomplished, although we cannot avoid
differences induced by the different nature of the metal atoms;
particularly important is the different mass and the different
momentum which may affect the migration phenomenon on the
4 (a) L. Abis, D. Belli Dell’Amico, C. Busetto, F. Calderazzo, R. Caminiti,
C. Ciofi, F. Garbassi and G. Masciarelli, J. Mater. Chem., 1998, 8, 751;
(
b) L. Abis, D. Belli Dell’Amico, C. Busetto, F. Calderazzo, R. Caminiti,
F. Garbassi and A. Tomei, J. Mater. Chem., 1998, 8, 2855; (c) L. Abis, L.
Armelao, D. Belli Dell’Amico, F. Calderazzo, F. Garbassi, A. Merigo
and E. A. Quadrelli, J. Chem. Soc., Dalton Trans., 2001, 2704.
5 (a) D. Belli Dell’Amico, F. Calderazzo, C. Ciofi, F. Garbassi, L.
Grande and G. Masciarelli, J. Cluster Sci., 1998, 9, 473; (b) A. Merigo,
Ph.D. Thesis, University of Pisa, 2000.
23
surface of the support. Previous suggestions have been made that
palladium should possess a catalytic activity similar to, or even
higher than, that of platinum in hydrogenation reactions. However,
6 (a) B. P. Andreini, D. Belli Dell’Amico, F. Calderazzo and M. G.
Venturi, J. Organometal. Chem., 1988, 354, 357, and references therein;
24
earlier papers have reported conflicting evidence about this point.
It is important to point out that both platinum and palladium
crystallize in the fcc structure and that the corresponding atomic
(
b) F. Bagnoli, D. Belli Dell’Amico, F. Calderazzo, U. Englert, F.
Marchetti, A. Merigo and S. Ramello, J. Organomet. Chem., 2001,
22, 180, and references therein.
6
˚
radii (for CN = 12) have similar values (A): platinum, 1.39;
7 (a) D. Belli Dell’Amico and F. Calderazzo, Inorg. Chem., 1981, 20,
1310; (b) D. Belli Dell’ Amico, F. Calderazzo and N. Zandon a` , Inorg.
Chem., 1984, 23, 137.
CRC Handbook of Chemistry and Physics, 82nd edn, ed. D. R. Lide,
Boca Raton, 2001–2, pp. 9–63.
25
palladium, 1.37. Thus, metal particles of the same dimensions
should contain the same number of atoms and the same percentage
of exposed atoms. In our case the average diameters of the metal
particles in the platinum- and palladium-loaded silica used in the
catalytic tests are 1.6 and 4.5 nm, respectively. It follows that
the percentage of exposed metal atoms should be about 60 and
8
9 S. Ramello, Chemistry Degree Thesis, University of Pisa,
996.
0 I. V. Fedoseev and A. S. Gordeev, Zh. Neorg. Khim., 2007, 52,
2; I. V. Fedoseev and A. S. Gordeev, Chem. Abstr., 2007, 148,
134337.
1
1
1
3
0% in the platinum and palladium samples, respectively. Thus,
the apparent lower activity of palladium can be attributed to a
morphological aspect rather than to an intrinsic property. We can
therefore confirm the conclusions by Boudart that the catalytic
activity of the two metals is similar.
11 (a) G. Booth, J. Chatt and P. Chini, Chem. Commun., 1965, 639; (b) G.
Booth and J. Chatt, J. Chem. Soc. A, 1969, 2131.
1
2 (a) P. L. Goggin and R. J. Goodfellow, J. Chem. Soc., Dalton Trans.,
973, 2355; (b) A. Modinos and P. Woodward, J. Chem. Soc., Dalton
Trans., 1975, 1516.
23
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