By means of spin-polarized density functional theory (DFT) computations, we unravel the reaction mechanisms of catalytic CO oxidation on B-doped fullerene. It is shown that O2 species favors to be chemically adsorbed via side-on configuration at the hex-C-B site with an adsorption energy of -1.07 eV. Two traditional pathways, Eley-Rideal (ER) and Langmuir-Hinshelwood (LH) mechanisms, are considered for the CO oxidation starting from O2 adsorption. CO species is able to bind at the B-top site of the B-doped fullerene with an adsorption energy of -0.78 eV. Therefore, CO oxidation that occurs starting from CO adsorption is also taken into account. Second reaction of CO oxidation occurs by the reaction of CO + O → CO2 with a very high energy barrier of 1.56 eV. A trimolecular Eley-Rideal (TER) pathway is proposed to avoid leaving the O atom on the B-doped fullerene after the first CO oxidation. These predictions manifest that boron-doped fullerene is a potential metal-free catalyst for CO oxidation.
By means of spin-polarized density functional theory (DFT) computations, we unravel the reaction mechanisms of catalytic CO oxidation on B-doped fullerene. It is shown that O2 species favors to be chemically adsorbed via side-on configuration at the hex-C-B site with an adsorption energy of -1.07 eV. Two traditional pathways, Eley-Rideal (ER) and Langmuir-Hinshelwood (LH) mechanisms, are considered for the CO oxidation starting from O2 adsorption. CO species is able to bind at the B-top site of the B-doped fullerene with an adsorption energy of -0.78 eV. Therefore, CO oxidation that occurs starting from CO adsorption is also taken into account. Second reaction of CO oxidation occurs by the reaction of CO + O → CO2 with a very high energy barrier of 1.56 eV. A trimolecular Eley-Rideal (TER) pathway is proposed to avoid leaving the O atom on the B-doped fullerene after the first CO oxidation. These predictions manifest that boron-doped fullerene is a potential metal-free catalyst for CO oxidation.
Catalytic CO oxidation
reaction has attracted considerable attention
due to its significance in purifying environmental pollution and eliminating
electrode poisoning in fuel cells.[1−5] CO oxidation is a simple and prototypical reaction and is suitable
for unraveling the intrinsic reaction mechanism of heterogeneous catalysis.[6,7] How to effectively detect and remove CO has been one of the most
challenging subjects nowadays. Conversion of CO into nontoxic substances,
CO2, by catalytic oxidation process has been extensively
studied using noble metals (Au,[8−12] Ag,[13] Pd,[14−16] Ru, Rh, Os, Ir,[14] and Au–Pd[17,18]) and metal
oxides (TiO2-,[19] CeO2-,[20−23] and ZrO2-based materials[24]) as excellent catalysts toward CO oxidation. However, their high
cost and scarcity have limited their applications. As a result, development
of nonmetal or metal-free catalysts to reduce or replace the use of
those metals in a large-scale process has become urgent.Carbon
nanomaterials, such as fullerenes, carbon nanotubes, graphenes,
etc., have been used widely as either catalyst supports or catalysts
for heterogeneous catalytic reaction. There have been several studies
on single-atom catalysts (SACs) supported on carbon nanomaterials,
for example, Pt-,[25−27] Cu-,[28] Fe-,[29] and Au-graphene,[30] and Fe-BN-fullerene,[31] which efficiently
catalyze oxidation of CO. The activation energy for the rate-determining
step (RDS) of CO oxidation on the above catalysts is predicted to
be within 0.51–0.58 eV, which is comparable to those of metal
catalysts. Doping heteroatoms (N, B, P, S, etc.) into carbon nanomaterials
could result in electron modulation to modify the electronic properties
and chemical activities that make heteroatom-doped carbon materials
potential catalysts for CO oxidation.[32−38] Previous investigations have shown that N-doped fullerene,[39] N-doped carbon nanotube,[40,41] N-doped penta-graphene,[42−44] graphdiyne,[45] B-doped and fullerene-like BN cage,[46] B-doped carbon nanotube,[47] and
so on can serve as metal-free catalysts and exhibit superior catalytic
activity toward CO oxidation. Unraveling the detailed reaction mechanisms
of CO oxidation is essential to design novel metal-free catalysts.
Boron-doped carbon nanotubes have been shown to exhibit high catalytic
activity both experimentally and theoretically.[47,48] Previous studies demonstrated that the energy barrier of RDS for
CO oxidation on B-doped fullerene using the Eley–Rideal (ER)
mechanism is predicted to be 0.48 eV.[49,50] They also
showed that second CO oxidation occurs by the reaction of CO with
the remaining O atoms, which have an energy barrier of 1.47 eV, which
limits its occurrence. To solve this issue, a trimolecular Eley–Rideal
(TER) pathway is proposed to avoid leaving the O atom on the B-doped
fullerene after the first CO oxidation, and it will be discussed below.
Understanding the intrinsic mechanisms of CO oxidation is important
to guide researchers to design the most effective catalyst.Herein, we carry out spin-polarized first-principles calculations
to unravel the catalytic mechanisms of CO oxidation on B-doped fullerene.
In this study, diverse mechanisms of CO oxidation reaction on B-doped
fullerene are revealed. The best reaction pathway of CO oxidation
is verified by discussing the energy barrier of the RDS.
Results and Discussion
Interaction
and Adsorption Behavior of O2 and CO
on B-doped Fullerene
To unravel the reaction mechanisms of
CO oxidation on B-doped fullerene, we first investigate the adsorption
behavior of O2 and CO on B-doped fullerene. A polarized
C––B+ bond, which becomes an active
site for molecular adsorption, is created by doping the boron atom
into fullerene (see Figure ). Gao and Chen have demonstrated that B-doped fullerene can
resist temperatures up to 1000 K, suggesting its structural stability.[50] Bader charge calculation shows that the carbons
bound to boron gain negative charges of 0.88–1.16 |e| from the substitutive boron. The O2 and CO
species are placed above those C–B sites containing B-top,
hex-C–B, and pent-C–B sites of the B-doped fullerene
at a proper distance during the geometric optimizations.
Figure 1
Optimized model
structures, possible active sites, and Bader charge
of B-doped fullerene. The gray and pink spheres represent C and B
atoms, respectively. The charges are given in |e|.
Optimized model
structures, possible active sites, and Bader charge
of B-doped fullerene. The gray and pink spheres represent C and B
atoms, respectively. The charges are given in |e|.The optimized configurations of O2 and
CO adsorption
on the B-doped fullerene as well as the related adsorption energies
are displayed in Figure and Table . It is
found that O2 species chemisorbs on the C–B site
of the B-doped fullerene via two types of configurations: side-on
and end-on configurations. Calculations demonstrate that the O2 species prefers to strongly chemisorb at the hex-C–B
site via the side-on configuration. The adsorption energy is computed
to be −1.07 eV, while those are −0.61 and −0.63
eV for the O2 side-on configuration at the pent-C–B
site and the O2 end-on configuration at the B-top site,
respectively. The related distance of O–O bond is calculated
to be elongated from 1.222 Å of free O2 molecule to
1.462, 1.461, and 1.318 Å, respectively, as depicted in Figure . Bader charge analysis
(see Table ) shows
that the adsorbed O2 species gain −1.42, −1.33,
and −1.28 |e| from the B-doped fullerene,
indicating that the O2 species is chemisorbed on the B-doped
fullerene. It is comparable to those on the catalysts of metals and
SACs, Pt surfaces (−0.58 to −0.72 eV for (111),[51] −1.48 eV for (110),[52] and −1.30 eV for (001)[53]), Pt clusters (−0.72 eV for Pt2 and −1.08
eV for Pt3),[54,55] Au clusters (−0.24
eV for Au4,[55] ca. −0.50
eV for Au7 and Au9,[30] −0.60 eV for Au29,[10,56,57] −0.99 eV[17,58] for Au38), Pt-graphene (−1.34 eV),[25] Cu-graphene (−2.67 eV),[28] Fe-graphene
(−2.09 eV),[29] Au-graphene (−1.34
eV).[30]
Figure 2
Optimized structures of O2 and
CO adsorption on B-doped
fullerene. The gray, pink, and red spheres represent C, B, and O,
atoms, respectively. The distances are given in angstroms.
Table 1
Computed Adsorption Energies (eV)
and Bader Charges (|e|; in Parentheses) of O2 and CO Species on the B-doped Fullerene
adsorbate/site
hex-C–B
penta-C–B
B-top
O2
–1.07 (−1.42)
–0.61 (−1.33)
–0.63 (−1.28)
CO
–0.78 (−0.49)
Optimized structures of O2 and
CO adsorption on B-doped
fullerene. The gray, pink, and red spheres represent C, B, and O,
atoms, respectively. The distances are given in angstroms.For the CO adsorption,
CO is placed at the mentioned active sites
with a 1.5–2.0 Å distance away from the B-doped fullerene
during structural optimization. One should note that CO species is
able to adsorb at the B-top site of the B-doped fullerene with an
adsorption energy of −0.78 eV. Compared to the cases of B-doped
carbon nanotube[47] and N-doped fullerene[59] (−0.05 and −0.20 eV for B-doped
carbon nanotube and N-doped fullerene, respectively), CO is chemisorbed
on the B-doped fullerene. More charge transfer (−0.49 |e|) from the B-doped fullerene occurs, resulting in stronger
interaction between the O2 species and the B-doped fullerene.
This result indicates that CO is likely to bind to B-doped fullerene.
The O adsorption, which is depicted in Figure S1, takes place by the first oxidation reaction of CO + O2 → CO2 + O. It is found that the atomic
O prefers to bind at the C–B site with the computed adsorption
energies of −5.10 and −5.24 eV at the penta-C–B
and hex-C–B sites, respectively.The minimum-energy paths
of O2 and CO adsorption at
B-doped fullerene have been illustrated by CINEB calculation, as depicted
in Figure S2. The calculation shows that
no energy barrier is required to surmount for the CO adsorption process,
but it needs a barrier of 0.2 eV to surmount for the O2 adsorption process, indicating that the CO adsorption process is
kinetically more favored than the O2 adsorption process,
which is thermodynamically favored. Therefore, CO oxidation process
occurs starting from both O2 and/or CO adsorption, as discussed
the following section.
CO Oxidation Reaction Starting from O2 Adsorption
and/or CO Adsorption on B-doped Fullerene
Here, we illustrate
the mechanisms of CO oxidation beginning from O2 adsorption
and/or CO adsorption on B-doped fullerene. Two traditional pathways,
Eley–Rideal (ER) and Langmuir–Hinshelwood (LH) mechanisms,
are considered for the CO oxidation.
CO Oxidation Starting from
the O2 Side-On Adsorption
The potential energy
surface (PES) of the CO oxidation reaction
via the LH mechanism at the hex-C–B site of B-doped fullerene
is mapped by the CINEB method, as described in Figure . The first step occurs by attachment of
the gas-phase CO molecule to fullerene to achieve O2 and
COco-adsorption (intermediate C) on the fullerene. The step is found
to be exothermic by 4.24 eV with an energy barrier of 0.51 eV. The
O–O bond distance in the O2 and COco-adsorption
(intermediate C) is found to increase to 2.154 from 1.461 Å.
Then, CO2 desorption takes place from the intermediate
C with a small energy barrier of 0.08 eV and an exothermicity of 0.58
eV. The overall reaction of O2 + CO → CO2 + O on the B-doped fullerene is exothermic by ∼5.00 eV and
requires to surmount a 0.51 eV barrier of the rate-determining step.
The second CO oxidation takes place by the remaining O atom on fullerene,
which will be studied below.
Figure 3
Energy diagrams for CO oxidation starting from
the O2 side-on adsorption via the LH mechanism at the hex-C–B
site
of B-doped fullerene.
Energy diagrams for CO oxidation starting from
the O2 side-on adsorption via the LH mechanism at the hex-C–B
site
of B-doped fullerene.Furthermore, the ER mechanism
is also discussed beginning from
the O2 side-on adsorption based on the PES depicted in Figure . The process begins
by the attachment of a gas-phase CO molecule to insert into the O–O
bond of the O2 end-on adsorption to form a carbonate-like
CO3 (intermediate C) with a large exothermicity of 4.57
eV. In TS B, the O–O bond is slightly elongated to 1.472 from
1.461 Å with 0.34 eV higher in energy than the reactant A. Subsequently,
CO2 desorption can occur by cleavage of Bfullerene–O and Cfullerene–O bonds with very high
barriers of 2.36 and 1.95 eV, respectively. The high barrier of this
process suggests that it is kinetically unfavored. To solve this issue,
a trimolecular Eley–Rideal (TER) pathway, reaction of the second
CO species with the CO3 intermediate, is proposed and will
be discussed below.
Figure 4
Energy diagrams for CO oxidation starting from the O2 side-on adsorption via the ER mechanism at the hex-C–B
site
of B-doped fullerene.
Energy diagrams for CO oxidation starting from the O2 side-on adsorption via the ER mechanism at the hex-C–B
site
of B-doped fullerene.
CO Oxidation Starting from
the O2 End-On Adsorption
First, the LH mechanism
is discussed beginning from the O2 end-on adsorption, as
depicted in Figure . The CO species initially approaches the
B-doped fullerene and interacts with the O2 end-on adsorption
to form a peroxo-type (OOCO) intermediate with an exothermicity of
2.03 eV, as seen in Figure . This step only requires 0.24 eV to surmount. The O–O
bond length is predicted to be elongated to 1.475 from 1.314 Å
in the OOCO intermediate. Then, the cleavage of the O–O bond
in the OOCO intermediate takes place to desorb CO2 via
a transition structure (TS D), with a barrier of 0.89 eV and endothermicity
of 1.64 eV. In TS D, the cleavage of the O–O and C–C
distances is predicted to be 1.831 and 1.673 Å, respectively.
The overall reaction beginning from the O2 end-on adsorption
is exothermic by 3.67 eV and needs to overcome a 0.89 eV barrier of
the rate-determining step.
Figure 5
Energy diagrams for CO oxidation starting from
the O2 end-on adsorption via the LH mechanism at the B-top
site of B-doped
fullerene.
Energy diagrams for CO oxidation starting from
the O2 end-on adsorption via the LH mechanism at the B-top
site of B-doped
fullerene.The ER mechanism is further described
beginning from the O2 end-on adsorption, as depicted in
the PES (see Figure ). CO species in reactant A
achieves end-on O2 adsorption and extracts one O atom directly
by surmounting a TS B with an energy barrier of 0.64 eV to produce
the final state C (product). In TS B, the O–O bond increases
from 1.318 to 1.330 Å, and the distance between the C atom of
CO and the O atom of O2 decreases from 2.705 to 2.333 Å.
The process is predicted to be highly exothermic by −5.01 eV.
The energy barrier (0.64 eV) of this rate-determining step is slightly
higher than that of the LH mechanism (0.51 eV).
Figure 6
Energy diagrams for CO
oxidation starting from the O2 end-on adsorption via the
ER mechanism at the B-top site of B-doped
fullerene.
Energy diagrams for CO
oxidation starting from the O2 end-on adsorption via the
ER mechanism at the B-top site of B-doped
fullerene.
CO Oxidation Starting from
the CO Adsorption
As mentioned
above, there is no energy barrier in the minimum-energy path for CO
adsorption at the B-top site of the B-doped fullerene with an adsorption
energy of −0.78 eV. Therefore, CO oxidation on the B-doped
fullerene starting from the CO adsorption can be achieved more easily
because this process is both kinetically and thermodynamically favored.
As seen in Figure , the gas-phase O2 species approaches the B-doped fullerene
and directly undergoes CO adsorption to form a peroxo-type (OOCO)
intermediate with an exothermicity of 0.99 eV. In addition, only a
low energy barrier of 0.05 eV is required for this step. The O–O
bond is found to increase to 1.490 from 1.238 Å in the OOCO intermediate.
Next, the cleavage of the O–O bond in the OOCO intermediate
occurs to desorb CO2 via a transition structure (TS D),
with a barrier of 0.39 eV and endothermicity of 3.40 eV. In TS D,
the cleavage O–O and C–B distances are computed to be
1.707 and 1.608 Å, respectively. The overall reaction beginning
from the CO adsorption is exothermic by 4.39 eV and needs to overcome
a 0.39 eV barrier of the rate-determining step. Compared to the proposed
reaction mechanisms beginning from the O2 adsorption as
alluded above, the energy barrier of the rate-determining step is
the lowest one (0.39 eV), indicating that CO oxidation prefers to
occur via the LH mechanism starting from the preadsorption of CO on
the B-doped fullerene.
Figure 7
Energy diagrams for CO oxidation starting from the CO
adsorption
via the LH mechanism at the B-top site of B-doped fullerene.
Energy diagrams for CO oxidation starting from the CO
adsorption
via the LH mechanism at the B-top site of B-doped fullerene.
Second CO Oxidation Occurring with the Remaining
O Atom
As depicted in Figures S3 and S4, the
gas-phase CO molecule approaches the adsorbed O species and undergoes
O adsorption to produce a second CO2 species. The process
via the ER mechanism (see Figure S3) is
exothermic by 1.03 eV but needs to pass a high energy barrier of 1.56
eV, while the process via the LH mechanism (see Figure S4) needs to overcome a high energy barrier of 1.82
eV. The desorption energy of CO2 is predicted to be 0.03
eV, suggesting that CO2 species is easily released from
the B-doped fullerene. However, the B-doped fullerene is readily poisoned
by the remaining O species due to the very high barrier for removing
the O atom. To solve this issue, a trimolecular Eley–Rideal
(TER) pathway is proposed to avoid leaving the O atom on the B-doped
fullerene after the first CO oxidation.
Trimolecular Eley–Rideal
(TER) Mechanism
In
this section, we consider the new TER mechanism of CO oxidation, which
is called the self-promotion mechanism proposed by Lyalin et al.,[60] to avoid leaving the O atom on the B-doped fullerene.
The TER mechanism can occur starting from the carbonate-like (CO3) and the peroxo-type (OOCO) intermediates. As shown in Figure , the second CO molecule
can approach the CO3 intermediate and extract one oxygen
in the CO3 to directly form two CO2 species
by passing barriers 1.37 eV (extracting the O atom bound to the B
atom) and 1.79 eV (extracting the O atom bound to C atom), which are
0.99 and 0.18 eV lower than 2.36 and 1.95 eV, respectively. The process
is more exothermic by 1.01 eV. The other TER mechanism can take place
through the OOCO intermediate depicted in Figure ; the second CO molecule can attach to the
OOCO intermediate and extract the O bound to B and/or C to produce
two CO2 species. The predicted energy barriers are 0.68
eV (extracting the O atom bound to the B atom) and/or 0.33 eV (extracting
the O atom bound to the C atom), which are 0.21 and 0.06 eV lower
than 0.89 and 0.39 eV for the traditional LH mechanism, respectively.
Besides, the process is more exothermic by 2.33 and 1.37 eV, respectively.
The calculation results demonstrate that the TER mechanism is found
to be more kinetical and thermodynamical compared with the traditional
LH and ER mechanisms.
Figure 8
Energy diagrams for CO oxidation starting from the carbonate-like
(CO3) intermediate via the TER mechanism.
Figure 9
Energy diagrams for CO oxidation starting from the peroxo-type
(OOCO) intermediate via the TER mechanism (a) starting from O2 end-on adsorption and (b) starting from CO adsorption.
Energy diagrams for CO oxidation starting from the carbonate-like
(CO3) intermediate via the TER mechanism.Energy diagrams for CO oxidation starting from the peroxo-type
(OOCO) intermediate via the TER mechanism (a) starting from O2 end-on adsorption and (b) starting from CO adsorption.The catalytic activity (energy barriers of the
rate-determining
step: 0.33–0.68 eV) of the B-doped fullerene via the TER mechanism
is comparable to those on the most studied catalysts including metal
surface system: Au(111) (1.97 eV)[13] and
Au(211) (0.59 and 0.65 eV);[9] metal nanoparticle
system: Au29 (0.69 eV),[10] Au38 (0.37 eV),[17] Pd38 (0.49
eV),[17] and core–shell Au–Pd
(0.10 and 0.59 eV for Au32/Pd6 and Pd32/Au6 clusters, respectively);[17] SAC system: Pt- (0.33 eV),[26,27] Cu- (0.54 eV),[28] Fe- (0.58 eV),[29] and
Au-embedded graphene (0.31 eV),[30] Fe-grapheneoxide (0.61 eV);[61] and metal-free catalysts:
N-doped fullerene (0.20 eV),[59] N-doped
(0.45–0.58 eV),[62] and B-doped CNTs
(0.34–0.42 eV).[47] Consequently,
the calculations suggest that B-doped fullerene could be an effective
metal-free catalyst for CO oxidation.
Conclusions
We
have investigated the detailed mechanisms for catalytic CO oxidation
catalyzed by the boron-doped fullerene by performing spin-polarized
first-principles calculations. The calculations demonstrate that O2 is chemisorbed via side-on configuration with adsorption
energies of −1.07 eV at the hex-C–B site of the boron-doped
fullerene. It is found that CO species can also bind at the B-top
site with an adsorption energy of −0.78 eV. There is no energy
barrier required to surmount for the CO adsorption process, but it
needs a barrier of 0.2 eV to surmount for the O2 adsorption
process, indicating that the CO adsorption process is kinetically
more favored than the O2 adsorption process. Therefore,
two traditional pathways, Eley–Rideal (ER) and Langmuir–Hinshelwood
(LH) mechanisms, are considered for the CO oxidation starting from
both O2 and/or CO adsorption. The results show that CO
oxidation takes place by the LH mechanism starting from the preadsorption
CO with the lowest energy barrier of 0.39 eV for the rate-determining
step. The remaining atomic O species continues to proceed second reaction
of CO oxidation with a very high energy barrier of 1.56 eV, which
hinders the catalytic activity of the B-doped fullerene. A TER pathway
is proposed to avoid leaving the O atom on the B-doped fullerene after
the first CO oxidation. The computations demonstrate that the TER
mechanism is found to be more kinetical and thermodynamical compared
with the traditional LH and ER mechanisms.
Computational Methods
All geometries are optimized using the periodic first-principles
computations based on spin-polarized density functional theory (DFT)
implemented in the Vienna Ab initio Simulation Package (VASP) code.[63,64] The exchange–correlation functional of Perdew–Wang
correlation (PW91) with the generalized gradient approximation (GGA)
is described.[65] The plane-wave basis set
is set to be 400 eV of cutoff energy. The Brillouin zones are selected
as Γ k-point mesh and 5 × 5 × 5 k-point mesh for geometric structure optimizations and electronic
property calculations, respectively.[66] A
25 × 25 × 25 Å3 periodic supercell is selected
for the calculations, which is large enough to avoid the interaction
of periodic images.[59] The adsorption energy
of adsorbates (O2 and CO) on B-doped fullerene is predicted
according to the following equationwhere Etot, EB-fullerene,
and Eadsorbate represent the computed
energies of adsorbed species
on the B-doped fullerene, the isolated B-doped fullerene, and the
gas-phase molecule, respectively. It is noted that the predicted O–O
bond lengths of gas-phase O2, C–O bond length of
gas-phase CO, and C–O bond length of gas-phase CO2 are 1.222, 1.137, and 1.169 Å, respectively, which agree with
the experimental data of 1.207,[67] 1.128,[68] and 1.193 Å.[69] The minimum-energy paths (MEP) including transition states are constructed
by the climbing image nudged elastic band (CINEB) method.[70,71] The electron distribution and transfer are described by the Bader
charge calculations.[72−74]
Authors: Janne T Hirvi; Toni-Jani J Kinnunen; Mika Suvanto; Tapani A Pakkanen; Jens K Nørskov Journal: J Chem Phys Date: 2010-08-28 Impact factor: 3.488
Authors: A Hornés; A B Hungría; P Bera; A López Cámara; M Fernández-García; A Martínez-Arias; L Barrio; M Estrella; G Zhou; J J Fonseca; J C Hanson; J A Rodriguez Journal: J Am Chem Soc Date: 2010-01-13 Impact factor: 15.419