38 research outputs found
Acrolein Hydrogenation on Ni(111)
Acrolein
hydrogenation via allyl alcohol, propanal, and enol into
propanol on the Ni(111) surface has been investigated using the spin-polarized
periodic density functional theory method. On the basis of the computed
adsorption energies and effective hydrogenation barriers, acrolein
hydrogenation into propanal and allyl alcohol obeys the LangmuirâHinshelwood
mechanism and propanal formation is more favored kinetically and thermodynamically
than allyl alcohol formation. Hydrogenation of propanal and allyl
alcohol should follow the EleyâRideal mechanism. The adsorption
energies of acrolein, allyl alcohol, and propanal along with the partial
hydrogenation selectivity on Ni, Au, Ag, and Pt catalysts have been
compared and discussed
Mechanisms of CO Activation, Surface Oxygen Removal, Surface Carbon Hydrogenation, and CâC Coupling on the Stepped Fe(710) Surface from Computation
To
understand the initial steps of Fe-based FischerâTropsch
synthesis, systematic periodic density functional theory computations
have been performed on the single-atom stepped Fe(710) surface, composed
by <i>p</i>(3 Ă 3) Fe(100)-like terrace and <i>p</i>(3 Ă 1) Fe(110)-like step. It is found that CO direct
dissociation into surface C and O is more favored kinetically and
thermodynamically than the H-assisted activation via HCO and COH formation.
Accordingly, surface O removal by hydrogen via H<sub>2</sub>O formation
is the only way. On the basis of surface CH<sub><i>x</i></sub> hydrogenation (<i>x</i> = 0, 1, 2, 3), surface CH<sub><i>x</i></sub> + CH<sub><i>x</i></sub> coupling
and CO + CH<sub><i>x</i></sub> insertion resulting in CH<sub><i>x</i></sub>CO formation followed by CâO dissociation,
surface C hydrogenation toward CH<sub>3</sub> formation is more favored
kinetically than the formation of CH<sub><i>x</i></sub>-CH<sub><i>x</i></sub> and CH<sub><i>x</i></sub>CO, as
well as thermodynamically. Starting from CH<sub>3</sub>, the formation
of CH<sub>4</sub> and CH<sub>3</sub>CO has similar barriers and endothermic
reaction energies, while CH<sub>3</sub>CO dissociation into CH<sub>3</sub>C + O has low barrier and is highly exothermic. Therefore,
turning the H<sub>2</sub>/CO ratio should change the selectivity toward
CâC formation and propagation
Reactions of CO, H<sub>2</sub>O, CO<sub>2</sub>, and H<sub>2</sub> on the Clean and Precovered Fe(110) Surfaces â A DFT Investigation
The reactions of CO and H<sub>2</sub>O on the clean Fe(110) surface
as well as surfaces with 0.25 monolayer O, OH, and H precoverage have
been computed on the basis of density functional theory (GGA-PBE).
Under the considerations of the reductive nature of CO as reactant
and H<sub>2</sub> as product as well as the oxidative nature of CO<sub>2</sub> and H<sub>2</sub>O, we have studied the potential activity
of metallic iron in the water-gas shift reaction. On the clean surface,
CO oxidation following the redox mechanism has a similar barrier as
CO dissociation; however, CO dissociation is much more favorable thermodynamically.
Furthermore, surfaces with 0.25 monolayer O, OH, and H precoverage
promote CO hydrogenation, while they suppress CO oxidation and dissociation.
On the surfaces with different CO and H<sub>2</sub>O ratios, CO hydrogenation
is promoted. On all of these surfaces, COOH formation is not favorable.
Considering the reverse reaction, CO<sub>2</sub> dissociation is much
favorable kinetically and thermodynamically on all of these surfaces,
and CO<sub>2</sub> hydrogenation should be favorable. Finally, metallic
iron is not an appropriate catalyst for the water-gas shift reaction
Mechanisms of Mo<sub>2</sub>C(101)-Catalyzed Furfural Selective Hydrodeoxygenation to 2âMethylfuran from Computation
The selective formation of 2-methylfuran
(F-CH<sub>3</sub>) and
furan from furfural (F-CHO) hydrogenation and hydrodeoxygenation on
clean and 4H precovered Mo<sub>2</sub>CÂ(101) surfaces has been systematically
computed on the basis of periodic density functional theory including
dispersion correction (PBE-D3). The clean Mo<sub>2</sub>CÂ(101) surface
has two distinct surface sites: unsaturated C and Mo sites for the
adsorption of H and furfural, respectively. The selectivity comes
from the different preference of furfural hydrogenation and dissociation
(F-CHO + H = F-CH<sub>2</sub>O vs F-CHO = F-CO + H) under the variation
of H<sub>2</sub> partial pressure. On the basis of the computed minimum
energy path on the clean surface, microkinetics shows that high H<sub>2</sub> partial pressure can promote 2-methylfuran formation and
suppress furan formation. To verify this proposed selectivity trend
of 2-methylfuran at high H<sub>2</sub> partial pressure, the 4H precovered
Mo<sub>2</sub>CÂ(101) surface (0.25 monolayer hydrogen coverage), which
provides neighboring hydrogens for promoting furfural hydrogenation
and blocks the active sites for suppressing furfural dissociation,
has been used. The computed results are in full agreement with the
experimentally observed selective formation of 2-methylfuran and the
H<sub>2</sub> reaction order of one half as well as rationalize the
need for a high H<sub>2</sub>/furfural ratio (400/1). On the basis
of these results, a new two-step protocol for experiments is proposed:
i.e., the first step is the pretreatment of the catalyst with hydrogen,
and the second step is furfural hydrogenation on H precovered catalysts
Formic Acid Dehydrogenation on Ni(111) and Comparison with Pd(111) and Pt(111)
Spin-polarized density functional theory calculations
have been
performed to investigate formic acid dehydrogenation into carbon dioxide
and hydrogen (HCO<sub>2</sub>H â CO<sub>2</sub> + H<sub>2</sub>) on Ni(111). It is found that formic acid prefers the O (Oî»C)
atop adsorption on nickel surface and the H (HâO) atom bridging
two neighboring nickel atoms, and formate prefers the bidentate adsorption
with O atop on nickel surface. The computed stretching frequencies
for deuterated formic acid (DCO<sub>2</sub>H) and deuterated formate
(DCO<sub>2</sub>) on Ni(111) agree well with the experimentally observed
IR spectra. Formic acid dehydrogenation into surface formate and hydrogen
atom (HCO<sub>2</sub>H â HCO<sub>2</sub> + H) has barrier of
0.41 eV and is exothermic by 0.35 eV. Formate dehydrogenation into
carbon dioxide and hydrogen atom (HCO<sub>2</sub> â CO<sub>2</sub> + H) has an effective barrier of about 1.0 eV and is the
rate-determining step. Our computed adsorption configurations and
energetic data for formic acid dehydrogenation on Ni(111) are very
close to the reported results for Pt(111), but in sharp contrast to
the previously reported results for Pd(111). Our recalculated adsorption
configurations and energetic data for formic acid dehydrogenation
on Pd(111) are similar to those on Ni(111) and Pt(111), demonstrating
the high similarities of these metals. These computed data show that
Pd-catalyzed formic acid dehydrogenation has the lowest effective
barrier (0.76 eV), followed by Ni (1.03 eV) and Pt (1.56 eV)
Rediscovering the Isospecific Ring-Opening Polymerization of Racemic Propylene Oxide with Dibutylmagnesium
Rediscovering the Isospecific Ring-Opening Polymerization
of Racemic Propylene Oxide with Dibutylmagnesiu
Mechanisms of H<sub>2</sub>O and CO<sub>2</sub> Formation from Surface Oxygen Reduction on Co(0001)
Surface
O removal by H and CO on Co(0001) has been studied using
periodic density functional method (revised PerdewâBurkeâErnzerhof
; RPBE) and ab initio atomistic thermodynamics. On the basis of the
quantitative agreement in the H<sub>2</sub>O formation barrier between
experiment (1.34 ± 0.07 eV) and theory (1.32 eV), H<sub>2</sub>O formation undergoes a consecutive hydrogenation process [O + 2H
â OH + H â H<sub>2</sub>O], while the barrier of H<sub>2</sub>O formation from OH disproportionation [2OH â H<sub>2</sub>O + O] is much lower (0.72 eV). The computed desorption temperatures
of H<sub>2</sub> and H<sub>2</sub>O under ultrahigh vacuum conditions
agree perfectly with the experiment. Surface O removal by CO has a
high barrier (1.41 eV) and is strongly endothermic (0.94 eV). Precovered
O and OH species do not significantly affect the barriers of H<sub>2</sub>O and CO<sub>2</sub> formation. All of these results indicate
that the present RPBE method and the larger surface model are more
suitable for studying cobalt systems
Synthesis and Catalytic Activity of [CpâČCo(COD)] Complexes Bearing Pendant NâContaining Groups
The novel CoÂ(I)-complex [Cp<sup>CN</sup>CoÂ(COD)] (Cp<sup>CN</sup> = η<sup>5</sup>-(C<sub>5</sub>H<sub>4</sub>CMe<sub>2</sub>CH<sub>2</sub>CN), COD = 1,5-cyclooctadiene; <b>3</b>) with
a substituted cyclopentadienyl ligand containing a pendant nitrile
moiety has been synthesized and characterized by X-ray diffraction.
The reactivity of the nitrile group in <b>3</b> has been investigated
regarding its behavior in cyclization reactions with alkynes, leading
to three new complexes containing pendant 2-pyridyl groups. All synthesized
complexes have been evaluated as catalysts in the [2 + 2 + 2] cycloaddition
reaction of 1,6-heptadiyne and benzonitrile
Toward Green Acylation of (Hetero)arenes: Palladium-Catalyzed Carbonylation of Olefins to Ketones
Green FriedelâCrafts acylation
reactions belong to the most
desired transformations in organic chemistry. The resulting ketones
constitute important intermediates, building blocks, and functional
molecules in organic synthesis as well as for the chemical industry.
Over the past 60 years, advances in this topic have focused on how
to make this reaction more economically and environmentally friendly
by using green acylating conditions, such as stoichiometric acylations
and catalytic homogeneous and heterogeneous acylations. However, currently
well-established methodologies for their synthesis either produce
significant amounts of waste or proceed under harsh conditions, limiting
applications. Here, we present a new protocol for the straightforward
and selective introduction of acyl groups into (hetero)Âarenes without
directing groups by using available olefins with inexpensive CO. In
the presence of commercial palladium catalysts, inter- and intramolecular
carbonylative CâH functionalizations take place with good regio-
and chemoselectivity. Compared to classical FriedelâCrafts
chemistry, this novel methodology proceeds under mild reaction conditions.
The general applicability of this methodology is demonstrated by the
direct carbonylation of industrial feedstocks (ethylene and diisobutene)
as well as of natural products (eugenol and safrole). Furthermore,
synthetic applications to drug molecules are showcased
Dissociative Hydrogen Adsorption on the Hexagonal Mo<sub>2</sub>C Phase at High Coverage
Hydrogen
adsorption on the primarily exposed (001), (100), (101), and (201)
surfaces of the hexagonal Mo<sub>2</sub>C phase at different coverage
has been investigated at the level of density functional theory and
using ab initio thermodynamics. On the Mo-terminated (001) and (100)
as well as mixed Mo/C-terminated (101) and (201) surfaces, dissociative
H<sub>2</sub> adsorption is favored both kinetically and thermodynamically.
At high coverage, each surface can have several types of adsorption
configurations coexisting, and these types are different from surface
to surface. The stable coverage as a function of temperature and partial
pressure provides useful information not only for surface science
studies at ultrahigh vacuum condition but also for practical applications
at high temperature and pressure in monitoring reactions. The differences
in the adsorbed H atom numbers and energies of these surfaces indicate
their different potential hydrotreating abilities. The relationship
between surface stability and stable hydrogen coverage has been discussed