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Hydrocarbon Oxidation
The conversion of hydrocarbons on oxides is being studied by
adsorbing hydrocarbon moieties on model surfaces prepared in-situ under
vacuum. The selective oxidation of alkyl groups in particular is
being explored by using alkyl iodides as suitable precursors. For
instance, the oxidation of 2-propyl moieties has been found to lead to
some acetone production on Ni(100) surfaces partially covered with
oxygen [N. R. Gleason and F. Zaera, J. Catal. 169 (1997) 365; F. Zaera,
N. R. Gleason, B. Klingenberg, A. H. Ali, J. Mol. Catal. 146 (1999)
13]. ISS data strongly suggest preferential bonding of the
hydrocarbon moiety to Ni sites [N. R. Gleason and F. Zaera, Surf. Sci.
385 (1997) 294], and RAIRS results point to a facile oxygen insertion
into the metal-alkyl bond to generate 2-propoxide intermediates [F.
Zaera, J. M. Guevremont and N. R. Gleason, J. Phys, Chem. B 105 (2001)
2257].
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Evidence for the first of the two steps
responsible for the oxidation of 2-propyl groups to acetone on an
oxygen-treated Ni(100) single-crystal surface.
Reflection-absorption infrared spectroscopy (RAIRS) data is provided to
highlight the early insertion of an oxygen atom into the metal-carbon
bond to form an alkoxide intermediate; notice in particular the
development of the C–O stretching vibration about 1100 cm-1. This
reaction appears to take place at temperatures as low as 200 K.
The data also indicate that the partial oxidation reaction can be
enhanced by prior deposition of hydroxyls on the surface, as those
groups lead to an increase in IR signal intensities (middle
spectrum). The top trace corresponds to the reactivity of
2-propanol on the same surface, and was used to help in the
identification of the 2-propoxide intermediate.
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The 2-propoxide moieties are stable on the surface up to ~325
K, at which point some undergo a rate-limiting beta-hydride elimination
to yield acetone [N. Gleason, J. Guevremont and F. Zaera, J. Phys.
Chem. B 107 (2003) 11133]. Other TPD experiments indicate that
propene does not react directly to yield acetone on O/Ni(100) surfaces,
a surprising result given that this is the pathway believed to be
followed on many oxide catalysts. The role of both subsurface
oxygen and hydroxide groups has been probed as well [N. R. Gleason and
F. Zaera, in 3rd World Congress on Oxidation Catalysis (Elsevier
Studies in Surface Science and Catalysis Series, Vol. 110), R. K.
Grasselli, S. T. Oyama, A. M. Gaffney and J. E. Lyons, editors,
Elsevier, Amsterdam, 1997, pp. 235-244; F. Zaera, Catal. Today 81
(2003), 149].
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Evidence for the second of the two-step
mechanism responsible for the oxidation of 2-propyl groups to acetone
on an oxygen-treated Ni(100) single-crystal surface, namely, a
beta-hydride elimination from 2-propoxide intermediates to yield
acetone. The production of acetone is indicated by its desorption
above 300 K in these TPD traces. Notice also the larger yield in
the TPD results from the hydroxyl-covered surface shown in the middle
trace. The corresponding data for 2-propanol is again provided to
illustrate the similar chemistry followed by the adsorbed alkyls and
alcohols, an observation that suggests that both react via the
formation of the same alkoxide intermediate.
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Newer studies have extended some of the main conclusions
reached with 2-propyl groups to other hydrocarbon moieties. In
particular, it has been clearly shown that both methyl [H. Guo and F.
Zaera, J. Phys. Chem. B 108 (2004) 16226] and methylene [H. Guo and F.
Zaera, Surf. Sci. 547 (2003) 299] groups can incorporate oxygen atoms
on nickel surfaces to yield oxygenates. In the case of methylene,
the direct result is formaldehyde desorption. With methyl
moieties, on the other hand, surface methoxide groups form prior to
their beta-hydride elimination to the aldehyde. This work has
also shown that both methyl and methylene groups not only couple
directly on NiO surfaces, but also grow small amounts of C3 and C4
hydrocarbons, most likely via methylene insertion steps. These
results may have profound implications for methane oxidative coupling
catalytic processes, as they suggest a possible Fisher-Tropsch
mechanism to produce heavier hydrocarbons.
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Schematic representation of the reaction
mechanism for the thermal chemistry of diiodomethane coadsorbed with
oxygen on Ni(110) surfaces. Highlighted are the stepwise loss of
iodine atoms in the adsorbed CH2I2, a chain growth mechanism based on
methylene insertion into nickel-alkyl bonds followed by fast
beta-hydride and reductive eliminations, the direct coupling of two
surface methylene groups to yield ethylene, an oxygen insertion to
produce formaldehyde, and a sequence of methylene insertions on
CH2I(ads) intermediates to eventually produce C3H5· and
C4H7· gas-phase radicals.
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Some catalytic kinetic work on the oxidation of hydrocarbons is being
performed in our laboratory as well [F. Zaera, N. R. Gleason, B.
Klingenberg, A. H. A. Ali, J. Mol. Catal.146 (1999) 13].
Specifically, the oxidation of alcohols on nickel wires and foils has
been investigated by using a micro-batch reactor [Ali H. Ali and F.
Zaera, J. Mol. Catal. A 177 (2002) 215]. We have shown that
partial oxidation products can be produced in significant quantities
under the right conditions. For instance, the reaction of
2-propanol with oxygen on nickel wires produced acetone almost
quantitatively as long as both the oxygen-to-hydrocarbon and the
reaction temperature are kept reasonably low. Primary alcohols
react in a somewhat less selective way, producing a small amount of the
corresponding acid as well as larger quantities of CO and CO2, but
significant yields of aldehydes are still possible under the right
conditions. The active surface in all these reactions appears to
be the thin nickel oxide film that forms immediately upon exposure of
nickel metal to the reaction mixture.
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Typical kinetic data for the partial
oxidation of alcohols by nickel catalysts. The data in this figure show
the dependence of the rate of oxidation of 2-propanol on the partial
pressure of oxygen over a Ni foil at 705 ± 2 K. The main
panel displays the raw data measured in a batch reactor, in the form of
the accumulation of acetone (in turnover numbers, TON =
molecules/Ni surface atom·s) as a function of reaction
time. The inset provides a Ln - Ln plot of the initial rates of
formation of acetone (in turnover frequencies, TOF = TON/time) versus
oxygen pressure, as calculated from the raw kinetic data. The
order of the reaction with respect to oxygen was estimated to be 0.51
± 0.05. These experiments prove that the partial
dehydrogenation of alcohols to aldehydes or ketones can be accomplished
with good selectivity by using nickel foils and oxygen-rich
mixtures. Similar results were obtained on silica-supported
nickel catalysts, but significant dehydration was seen on alumina-based
solids because of the acidity of that oxide.
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Additional kinetic and infrared characterization
experiments have been carried out on supported nickel catalysts.
The kinetic behavior seen on nickel foils was by and large reproduced
qualitatively on supported nickel catalysts. Indeed, nickel
particles deposited on neutral silica powders display similar high
selectivities towards alcohol dehydrogenation to aldehydes or
ketones. When alumina is used instead, however, significant
dehydration is seen as well. For instance, when using a
2-propanol:oxygen 2:1 mixture, the 70% selectivity for 2-propanol
dehydrogenation to acetone seen on a nickel foil goes down to only
about 30% on Ni/alumina. Additional transmission infrared (IR)
spectroscopy characterization studies allow for the identification of
most of the intermediates in these reactions. The figure below
shows a typical set of spectra for the thermal chemistry of 2-propanol
on a 10% nickel/alumina catalyst in the presence of gas-phase
oxygen. In this particular instance, it is clear that the
original alcohol decomposes to acetone between 440 and 450 K, but that
some acetate surface species are also produced under certain
conditions. In fact, in the case of ethanol on Ni/SiO2, ethoxide,
acetaldehyde, acetate, formate and CO2 were all sequentially identified
with increasing temperature. Finally, again, a thin and partially
oxidized layer (as identified by CO infrared probing experiments) seems
to optimize the partial oxidation.
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Transmission infrared absorption spectra
obtained during the thermal oxidation of 2-propanol on 10% Ni/Al2O3
after sequential exposures to 10 Torr of the alcohol and 10 Torr of
oxygen. A change in the nature of the adsorbed species is seen
about 440 K, from molecular adsorption to metal-adsorbed acetone, with
its characteristic IR bands around 1378, 1472, and 1590 cm-1 (the
symmetric and asymmetric methyl deformations and the carbonyl
stretching modes, respectively). Experiments such as these allow
for the identification of potential surface intermediates during
catalysis.
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The kinetics of the total oxidation of alkanes (methane,
ethane, propane, n-butane and iso-butane) over Ni, Pd, and Pt foils was
also studied under fuel-lean conditions by using the same
recirculating-loop batch reactor with mass spectrometry detection [M.
Aryafar and F. Zaera, Catal. Lett. 48 (1997) 173].
Researchers:
Funding:
Equipment: |
Mr. Min Shen, Dr. Hansheng Guo
Department of Energy - Basic Energy Sciences
UHV Chambers # 1 and #3
Batch Reactor |
Last modified on June 28, 2005
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