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Hydrocarbon Hydrogenation-Dehydrogenation
One of our long-term projects is to study the reaction
mechanism for the catalytic hydrogenation and dehydrogenation of
olefins and other unsaturated hydrocarbons. Our initial studies,
based mainly on the thermal chemistry of ethylene on Pt(111)
single-crystal surfaces [F. Zaera, Langmuir 12 (1996) 88; F. Zaera, T.
V. W. Janssens and H. Öfner, Surf. Sci. 368 (1996) 371; F. Zaera,
Isr. J. Chem. 38 (1998) 293], clearly showed that olefin hydrogenation
proceeds via the stepwise and reversible incorporation of hydrogen
atoms. However, it became apparent that while in vacuum these
reactions occur on the clean metal [F. Zaera, J. Phys. Chem. 94 (1990)
5090], under the atmospheric pressures typical in catalysis they take
place in the presence of a carbonaceous layer that grows on the surface
soon after its exposure to the reactant gases [F. Zaera and G. A.
Somorjai, J. Am. Chem. Soc. 106 (1984) 2288]. These strongly
bonded hydrocarbon fragments have been shown to consist of alkylidyne
moieties, the structure of which is exemplified for ethylidyne in the
figure below.
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Infrared and low-energy
electron diffraction evidence for the formation of ethylidyne from
room-temperature ethylene adsorbed on a Pt(111) surface. The
vibrational modes seen for the C-C stretching at 1118 cm-1, the
symmetric methyl deformation (umbrella mode) at 1339 cm-1, and the
symmetric C-H stretching at 2883 cm-1 are characteristic of ethylidyne
moieties. The structure of the carbon backbone of ethylidyne
determined by LEED experiments is shown in the inset.
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A careful study into the conversion of ethylene to ethylidyne
revealed the complex mechanism illustrated in the figure below.
Vinyl intermediates were ruled out because they themselves undergo a
series of side reactions to form a number of intermediates –including
ethylene– before ultimately transforming into ethylidyne [F. Zaera and
N. Bernstein, J. Am. Chem. Soc. 116 (1994) 4881]. The
participation of ethyl groups was also discarded on the grounds that
those decompose readily via beta-hydride elimination into ethylene [F.
Zaera, Surf. Sci. 219 (1989) 453; H. Hoffmann, P. R. Griffiths and F.
Zaera, Surf. Sci. 262 (1992) 141]. Lastly, the involvement of
ethylidene in a simple two-step mechanism was initially found to be
inconsistent with results from kinetic studies using trideuteroethylene
[F. Zaera, J. Am. Chem. Soc. 111 (1989) 4240], but later shown to be
possible if a fast ethylene-ethylidene pre-equilibrium were to precede
its slow decomposition to ethylidyne [T. V. W. Janssens and F. Zaera,
J. Phys. Chem. 100 (1996) 14118; F. Zaera and C. R. French, J. Am.
Chem. Soc. 121 (1999) 2239]. The involvement of alkylidenes in
this reaction has also been corroborated by the lack of dependence of
the rate of alkylidyne formation on the coverage of hydrogen on the
surface. Finally, the mechanism of the overall reaction was found
to change with surface coverage.

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The conversion of adsorbed olefins to alkylidynes competes
kinetically with other reactions. Of particular importance for
catalysis is the occurrence of H/D exchange and hydrogenation steps [T.
V. W. Janssens and F. Zaera, Surf. Sci. 344 (1995) 77]. H/D
exchange in particular was shown to take place via the interchange
between di-sigma adsorbed alkenes and alkyl intermediates, and to
require temperatures well below those needed for other steps [T. V. W.
Janssens, D. Stone, J. C. Hemminger and F. Zaera, J. Catal. 177 (1998)
284]. RAIRS kinetic experiments have pointed to the fact that the
extent of deuterium substitution during the formation of alkylidynes is
largely determined by the previous H/D exchange between ethylene and
surface hydrogen. It has also been observed that the dosing order
of the reactants influences the kinetics of the reaction, indicating
that specific surface ensembles are required: both the rate and the
degree of H/D exchange reaction can be increased by dosing hydrogen
prior to the olefin. All these data can be explained on the basis
of a mechanism in which the H/D exchange reaction and formation of
ethylidyne are parallel processes involving different surface species
(see above).
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Typical mass spectra from laser-induced
thermal desorption/Fourier-transform infrared spectroscopy experiments
designed to characterize the kinetics of H/D exchange reactions between
C2D4 and surface H on Pt(111). The exchange is manifested here
both by a decrease of the 32 amu signal (C2D4) and by the simultaneous
growth of the 31 (C2D3H) and 29 and 27 (multiply exchanged C2X4) amu
signals during the course of the reaction.
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The kinetics of the hydrogenation of ethylene to ethane on
Pt(111) was also studied isothermally under vacuum by using a variation
of the dynamic molecular beam method originally devised by King and
Wells [H. Öfner and F. Zaera, J. Phys. Chem. B 101 (1997) 396; H.
Öfner and F. Zaera, J. Am. Chem. Soc., 124 (2002) 10982].
The uptake of ethylene on platinum (111) single-crystal surfaces was
shown to involve two adsorption states, a di-sigma species irreversibly
bonded on the clean surface, and a second pi reversibly-adsorbed state
which develops at high coverages. The two states display
significantly different kinetic behavior, but can slowly interchange,
suggesting an initial adsorption on empty metal atoms in an imperfect
monolayer followed by a collective rearrangement of the neighboring
molecules into a new compressed layer. Direct infrared
spectroscopic evidence was obtained with propylene for the formation of
the second pi-bonded olefin [F. Zaera and D. Chrysostomou, Surf. Sci.
457 (2000) 71], and a reduction of the total ethylene uptake but an
increase the amount of the weakly-adsorbed ethylene with hydrogen
coadsorption was also proven. The first-order dependence measured
for the rate of ethylene hydrogenation on the coverage of this weakly
bonded species provided additional support for the idea of it being the
direct intermediate in the hydrogenation of ethylene. Finally,
the presence of ethylidyne on the surface was found irrelevant for the
hydrogenation reaction except for their blocking of surface sites.
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Typical isothermal kinetic data obtained
for the uptake of ethylene on Pt(111) at 270 K using a molecular beam
technique. The initial irreversible adsorption seen within the
first 20 s (blue points) is followed by an additional small reversible
adsorption of weakly (pi) bonded olefin (red points). A
comparison between the coverages of the strongly (di-sigma) and weakly
(pi) bonded ethylene and the initial rate of ethane formation indicate
that it is the latter weakly adsorbed ethylene the one involved in the
hydrogenation reaction. In fact, the formation of an analogous pi
species has been directly determined by infrared spectroscopy for the
case of propylene. The catalytic conversion of olefins on
supported metal catalysts is believed to involve a similar pi
adsorption on top of strongly adsorbed carbonaceous deposits.
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More complex reactions resulting from the sequential
hydrogenation-dehydrogenation steps between alkanes and alkenes can be
probed with heavier olefins. For instance, the participation of
allylic intermediates during hydrogenation or H/D exchange reactions
has been clearly ruled out using propylene on Pt(111) [F. Zaera and D.
Chrysostomou, Surf. Sci. 457 (2000) 89; 144. D. Chrysostomou, C. French
and F. Zaera, Catal. Lett. 69 (2000) 117;D. Chrysostomou and F. Zaera,
J. Phys. Chem. B 105 (2001) 1003]. Double-bond migration and
cis-trans isomerization has also been probed with butylene [I. Lee and
F. Zaera, J. Phys. Chem. B 109 (2005) 2745]. Particularly curious
is the fact that the isomerization of trans-2-butene to its cis
conformer was found to be easier on Pt(111) surfaces than the opposite
cis to trans conversion. This kinetic trend, which is opposite to
what would be expected on thermodynamic grounds, is explained by an
increased stability of the cis isomer upon adsorption. A model
where adsorption energies are affected by steric interactions between
the side moieties of the olefin and the surface suggests that
selectivity toward cis vs. trans formation may be manipulated by
controlling the structure of the surface of the catalyst.

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Energy diagram for the interconversion of butenes on metal
surfaces. Shown are the elementary steps responsible for
double-bond migration between 1-butene and 2-butene as well as for
cis-trans isomerization within 2-butene. Of particular importance
here is the role that the subtle relative differences among the energy
barriers of the different beta-hydride elimination steps from the
common 2-butyl surface intermediate play in defining the selectivity of
these reactions.
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Our H/D exchange studies have been extended to other compounds
[A. Loaiza, M. Xu and F. Zaera, J. Catal. 159 (1996) 127]. The
isotope exchange in ethane in particular has been studied over platinum
surfaces under catalytic conditions. A detailed analysis of the
resulting products always indicates a U-shaped distribution, with
maxima at the singly- and fully-deuterated ethane molecules [F. Zaera
and G. A. Somorjai, J. Phys. Chem., 89 (1985) 3211]. Additional
13C-NMR [A. Loaiza, D. Borchardt and F. Zaera, Spectrochim. Acta A, 53
(1997) 2481] and high-resolution and tandem mass spectrometry [A.
Loaiza and F. Zaera, J. Am. Soc. Mass Spectrom. 15 (2004), 1366]
analysis has also pointed to the preferential formation of CH2D-CH2D
over that of CH3CHD2, suggesting that adsorbed ethylene is one of the
main intermediates in the mechanism for the complete exchange.
The chemistry observed has been explained on the basis of a sequence of
steps including the formation of ethyl, ethylene, and ethylidyne
surface intermediates.

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| 13C NMR
analysis of a mixture obtained after the catalytic H-D exchange
between normal ethane and D2 over a platinum foil. The use of
this
technique allows for the identification of all possible isotopic
substitutions in the ethane molecule, and provides specific information
about the regioselectivity for the exchange reaction. The data
not
only show that there are two competing mechanisms responsible for mono
and perdeutero exchange, respectively, but also prove that the latter
involves the formation of a chemisorbed ethylene intermediate. |
Lastly, initial experiments have also been carried out with more
complex molecules such as unsaturated aldehydes [J. C. de Jesús
and F. Zaera, J. Mol. Catal. A 138 (1999) 237; J. C. de Jesús
and F. Zaera, Surf. Sci. 430 (1999) 99]. The main thermal
decomposition path seen for both acrolein and crotonaldehyde was the
expected decarbonylation of the unsaturated aldehyde to carbon monoxide
and the corresponding olefin (ethene and propene, respectively), but
small amounts of propene and ketene were detected in the case of
acrolein as well. The RAIRS data indicates that while acrolein
initially adsorbs with its plane parallel to the surface and interacts
mainly via the carbonyl group, crotonaldehyde adopts a more complex
geometry where the main interaction to the metal is via a
rehybridization of the C=C double bond. It is suggested here that
the changes in adsorption geometry induced by substitutions in the C=C
double bond may be responsible for the observed changes in the
subsequent reactivity of the adsorbed unsaturated aldehydes, an idea
that we plan to explore in more detail. We are also interested in
looking at the details of asymmetric hydrogenation catalysis.
Researchers:
Funding:
Equipment:
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Dr. Ilkeun Lee
National Science Foundation - Chemistry Division
UHV Chambers #2 and #3
Batch Reactor |
Last modified on June 27, 2005
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