Abstract

On the basis of density functional theory calculations, we explored the catalytic properties of various heteroatom-doped black and gray arsenene toward the oxygen reduction reaction (ORR), the oxygen evolution reaction (OER), and the hydrogen evolution reaction (HER). The calculation results show that pristine black (b-As) and gray arsenene (g-As) exhibit poor catalytic performance because of too weak intermediate adsorption. Heteroatom doping plays a key role in optimizing catalytic performance. Among the candidate dopants O, C, P, S, and Sb, O is the most promising one used in arsenene to improve the ORR and OER catalytic performance. Embedding O atoms could widely tune the binding strength of reactive intermediates and improve the catalytic activity. Single O-doped g-AsO1 can achieve efficient bifunctional activity for both the OER and the ORR with optimal potential gap. b-AsO and b-AsO2 exhibit the optimal OER and ORR catalytic performance, respectively. For the HER, double C-doped g-AsC could tune the adsorption of hydrogen to an optimal value and significantly enhance the catalytic performance. These findings indicate that arsenene could provide a new platform to explore high-efficiency electrocatalysts.
Introduction
The development of effective catalysts for the oxygen reduction reaction (ORR), the oxygen evolution reaction (OER), and the hydrogen evolution reaction (HER) are highly desirable for new clean energy technologies. Nowadays, various two-dimensional (2D) layered materials have been extensively explored as high-performance catalysts, including heteroatom-doped graphene for the ORR and OER,1,2 black phosphorus (BP) for the OER,3−5 MoS2 and SnS2 for the HER,6,7 transition-metal-anchored C2N for the HER and OER,8 etc.9,10
Recently, elemental 2D layered arsenic (As) of the same group V element as P has attracted extensive attention due to its unique electronic and structural properties. Arsenic exists in two most widely studied allotropes: black arsenic and gray arsenic.11−14 As a cousin of BP, black arsenic also possesses the orthorhombic puckered honeycomb structure.11,12 Gray arsenic has the same hexagonal buckled geometry as blue phosphorus.12 Some studies have verified that black arsenic shows anisotropic and thickness-dependent semiconductor characteristics.15,16 Upon reducing the layer numbers to the monolayer, black arsenic exhibits the transformation of the direct–indirect band gap,17 while gray arsenic exhibits the transformation from semimetals to semiconductors.18 More importantly, black and gray arsenic monolayers (arsenene) have been predicted to possess high carrier mobility,15,16,19 which will accelerate the electron transport of the electrocatalytic reaction. Black and gray arsenene also possess a relatively good environmental stability that is critical for catalytic durability.16 On the basis of these distinct properties, arsenene has shown great potential for many emerging applications, including thermoelectric applications20,21 and field-effect transistors.16 In addition to the above applications, these excellent structural and electronic characteristics may also endow arsenene with potential catalytic application for the ORR, OER, and HER.
Pristine black and gray arsenene could also be chemically modified to exhibit superior structural and electronic properties. For example, Sturala et al. have predicted that through chemical modification of the surface, multilayer and monolayer arsenic materials can obtain large surface coverage and high luminescence.22 Li et al. have suggested that by doping heteroatoms B, C, N, O, etc., gray arsenene can realize tunable electronic structures and magnetic properties, which indicates that doped gray arsenene will possess promising potential for applications in electronics and spintronics.23 In addition, it was reported that O-dopant-modified black arsenene can act as an effective HER electrocatalyst with high catalytic activity.24 Therefore, we believe that impurity doping could greatly tune the catalytic activities of black and gray arsenene. Although great progress has been made in investigating the geometric structures and electronic properties of pristine and impurity-doped arsenene, experimental and theoretical research toward the ORR, OER, and HER of heteroatom-doped black and gray arsenene materials has never been reported.
In this work,
based on density functional theory (DFT) calculations,
the ORR, OER, and HER catalytic performances of heteroatom-doped black
arsenene (b-As) and gray arsenene (g-As) have been studied. The results
show that O atoms are more easily embedded into the arsenene lattice
than other heteroatoms, especially for double O-atom doping. By calculating
the overpotentials of the ORR/OER processes and the Gibbs free energy
of H* adsorption for the HER, we find that pristine b-As and g-As
exhibit poor catalytic activities. O and C dopants can effectively
tune the absorption strength of intermediates and thus enhance catalytic
activities. Single O-doped
is best suited for
the OER process, and
optimal ORR activities could be realized on double O-doped
. The reaction free
energies of H* could
be optimized to the appropriate value on double C-doped
, indicating improved
HER catalytic performance.
The present findings could provide a useful guidance for developing
multifunctional arsenene-based metal-free catalysts.
Computational Methods
First-principle calculations were performed within the framework of spin-polarized DFT, as implemented in the Vienna Ab Initio Simulation Package (VASP).25,26 The projector augmented wave pseudopotential is used to describe nuclei–electron interactions,27 while the electronic exchange–correlation corrections were described within the generalized gradient approximation, as parameterized by Perdew–Burke–Ernzerhof.28 A cutoff energy of 500 eV was used within the plane wave basis set. To evaluate the catalytic performance, we constructed 4 × 4 × 1 b-As and 5 × 5 × 1 g-As supercells, as shown in Figure S1. The Brillouin zone was sampled using a 5 × 5 × 1 Monkhorst–Pack grid centered at the gamma (Γ) point. All atoms in the cell are fully optimized until the force acting on each atom is less than 0.02 eV Å–1. A vacuum region of 15 Å is created in the slab model to neglect the interaction between adjacent models, and we employ the DFT-D3 scheme to describe the dispersion interaction between model surfaces and adsorbed intermediates.29,30
The formation energies Ef’S of substitutional atoms (O, C, P, S, and Sb) in b-As and g-As lattices are calculated by31,32
| 1 |
where Etot(m) and Etot are the total energies of the heteroatom-doped and pristine b-As/g-As surface, respectively; μAs is the chemical potential of As and is calculated from the bulk phase of As; μX is the chemical potential of the introduced X atoms (X = O, C, P, S, and Sb) and calculated as in O2, graphene, bulk phase of BP, alpha-S, and Sb, respectively; and m is the number of substituted X atoms in the model.
According to the standard hydrogen electrode method, the four-electron ORR and OER reaction progress is investigated in an acidic environment.33,34 The OER could occur along the following reaction paths:
| 2 |
| 3 |
| 4 |
| 5 |
where * stands for the absorption site on the catalyst surface; (l) and (g) indicate the liquid and gas phases, respectively; O*, OH*, and OOH* represent the adsorbed intermediates. The ORR reaction is the reverse process of the OER listed above from eqs 2–5.
The ORR and OER overpotentials (η’s) can be obtained by calculating the Gibbs free energy ΔG for each reactive step of eqs 2–5. ΔG is defined by the following equation:
| 6 |
The details of the parametric description in eq 6 and the calculation process for η’s are described in the Supporting Information.
The HER reaction progress is also investigated in an acidic environment, and the catalytic performance can be evaluated by calculating the Gibbs free energy ΔGH* of adsorbed hydrogen, defined as6
| 7 |
where ΔZPE and ΔS are the zero-point energy change and vibrational entropy correction and ΔEH* is the adsorbed energy of H* and can be calculated by10
| 8 |
where EH* and Esurface are the total energies
of the surface
with and without adsorbed H*, respectively, and
is
the total energy of the gas-phase H2 molecule. The vibrational
entropy of H* is negligible; hence,
, where
is
the entropy of H2 in the
gas phase under standard conditions, as shown in Table S1. Therefore, ΔGH* with the overall correction can be written as35
| 9 |
Results and Discussion
The ORR (ηORR) and OER (ηOER) overpotentials are usually used to characterize the ORR/OER catalytic performance, which can be obtained from the reaction free-energy diagrams.33,34,36Figure 1a,b displays the free-energy diagrams for the ORR/OER of pristine black arsenene (b-As) and gray arsenene (g-As) at different electrode potentials U. The forward (2H2O + * → O2) and backward (O2 → 2H2O + *) processes represent the OER and ORR, respectively. The overpotentials of ηOER and ηORR are denoted by blue and red arrows, and the adsorbed intermediates (O*, OH*, and OOH*) are displayed below each free-energy diagram. For the OER on pristine b-As in Figure 1a, at U = 1.23 V of the equilibrium potential shown in green lines, the transformations of OH* → O* and OOH* → O2 are downhill. However, elementary reaction steps of H2O → OH* and O* → OOH* both are uphill, and the highest free-energy gain of 1.85 eV for O* → OOH* has to be overcome. Only when U increases to 3.08 V, as shown in blue lines, can all reaction steps become downhill and occur spontaneously. Hence, 1.85 V is the OER overpotential ηOER and the step of O* → OOH* is the rate-determining step (RDS). For the ORR process, at U = 1.23 V, the step of O2 → OOH* possesses the highest free-energy gain of 2.49 eV, determining the ORR-RDS. As shown in the red lines, at U = −1.26 V, this free-energy gain will vanish and all steps are downhill, corresponding to ηORR = 2.49 V. Similarly, for pristine g-As in Figure 1b, the RDSs of the OER and ORR also arise from O* → OOH* with ηOER = 1.72 V and from O2 → OOH* with ηORR = 2.40 V, respectively, which are mainly attributed to the weak adsorption of the intermediate OOH*. According to the Sabatier principle, the catalytic activities strongly depend on the adsorption strength of intermediates, which should be not too weak nor too strong for an effective catalyst.37 Too weak adsorption will result in an inefficient reaction, while too strong adsorption of the intermediates will gradually terminate the reaction by blocking the catalytic active sites. The calculated high OER and ORR overpotentials in Figure 1 indicate that pristine b-As and g-As could not act as effective catalysts.
Figure 1.
Free-energy diagrams for OER and ORR elementary steps on pristine (a) black and (b) gray arsenene at different electrode potentials U. The atomic structures (top and side views) of the adsorbed intermediates O*, OH*, and OOH* are also shown below each diagram.
To improve the catalytic properties of b-As and
g-As, we employ
chemical modification by embedding a variety of heteroatoms including
O, C, P, S, and Sb into the arsenene lattice. The calculated formation
energies Ef’s for different kinds
of X-doped (X = O, C, P, S, and
Sb) b-As and g-As are presented in Figure 2a. For each heteroatom, two types of configurations
with a single dopant and double dopants are calculated. The more negative
value of Ef corresponds to more stable
doping configurations. As shown in Figure 2a, compared to other heteroatoms, O atom
doping exhibits a relatively smaller Ef value whether for a single dopant and double dopants, indicating
that it is more likely to be embedded into b-As and g-As lattices
than other heteroatoms. Furthermore, Ef’s of double O-doped
and
are smaller than those
of single O-doped
and
, which suggests that
the interaction with
each other between O atoms can further help stabilize defective configuration.
In addition, other double atom-doped configurations also exhibit a
negative Ef value, such as
,
, and
. Based on the above
analysis, in the following
discussion, we will focus on the catalytic properties for the ORR,
OER, and HER on O-doped b-As and g-As and add other stable heteroatom-doped
configurations for comparison. Figure 2b–e displays the atomic structures of respective
single and double O-doped b-As (
and
) and g-As (
and
). To further identify
the stability of
heteroatom-doped arsenene, we perform the ab initio molecular dynamic
simulations at a temperature of 300 K to examine the dynamic stability. Figure S2 shows the fluctuation of the total
energy during the MD simulations and the corresponding snapshots for
representative
,
, and
. Compared with the
initial snapshots at
0 ps, all structures exhibit slight changes at room temperature, suggesting
the high structural stability.
Figure 2.

(a) Formation energy for single and double
X-doped gray arsenene
(
and
) and black arsenene
(
and
) (X = C, O, P, S, and
Sb). O-doped atomic structures of (b)
, (c)
, (d)
, and (e)
. Purple, blue, and
red balls indicate As
atoms in black and gray arsenene, and O atoms, respectively.
Figure 3a shows
the calculated OER overpotentials ηOER’s at
different active sites for pristine and O-doped b-As/g-As. For comparison,
we add the overpotential data of C-doped b-As/g-As. Table 1 summarizes the calculated free
energies of the adsorbed intermediates and overpotentials in investigated
configurations, and atomic structures of O- and C-doped clusters with
detailed active sites are shown in Figure S3. As shown in Figure 3a, the ηOER’s of these structures exhibit
a typical volcano shape, suggesting that introducing heteroatoms can
tune the OER catalytic activity in a wide range. Obviously, pristine
b-As and g-As with high ηOER values of 1.85 and 1.72
V locate at the bottom of the OER volcano, indicating the poor OER
catalytic activity. In contrast, close to the peak of the volcano,
as shown by the red arrow, single O-doped
exhibits the lowest
ηOER of 0.71 V, indicating improved OER catalytic
activity. For O-doped
b-As, the optimal OER catalytic active site also locates on the single
O-doped configuration
with ηOER = 0.94 V, as
denoted by the blue arrow. In addition, it is worth noting that single
C-doped
shown by
the black diamond also locates
near the peak of the volcano, indicating excellent catalytic performance,
but it is very difficult to prepare
in experiments because
of its high Ef, as shown in Figure 2a. Therefore, we do not choose
as an effective OER
catalyst.
Figure 3.
(a) Volcano plots for the OER vs the difference between adsorption
energies of O* and OH* for single and double C- and O-doped b-As and
g-As. Free-energy diagrams for the optimal OER on (b)
and (c)
at U = 1.23 V. The corresponding
atomic structures of the adsorbed intermediate OOH* are shown in the
insets.
Table 1. Adsorption Energies of Intermediates (O*, OH*, and OOH*) in Electronvolt, Reaction Free Energies in Electronvolt of Each Reactive Step along the OER Reaction Pathway and OER/ORR Overpotentials in Volt at Different Active sites for C- and O-doped black and gray arsenenea.
| ΔGOH* | ΔGO* | ΔGOOH* | ΔG1 | ΔG2 | ΔG3 | ΔG4 | ηOER | ηORR | ||
|---|---|---|---|---|---|---|---|---|---|---|
![]() |
A | –0.30 | 1.11 | 2.97 | –0.30 | 1.41 | 1.86 | 1.94 | 0.71 | 1.53 |
| B | 0.95 | 1.64 | 4.38 | 0.95 | 0.69 | 2.74 | 0.54 | 1.52 | 0.68 | |
| C | 0.75 | 1.59 | 1.92 | 0.75 | 0.83 | 0.33 | 2.99 | 1.76 | 0.89 | |
![]() |
A | 0.74 | 1.15 | 4.10 | 0.74 | 0.40 | 2.95 | 0.81 | 1.72 | 0.82 |
| B | 1.19 | 1.44 | 4.44 | 1.19 | 0.25 | 2.99 | 0.47 | 1.76 | 0.97 | |
![]() |
A | –0.81 | 0.87 | 2.74 | –0.81 | 1.68 | 1.86 | 2.17 | 0.94 | 2.04 |
| B | –0.01 | 1.18 | 3.36 | –0.01 | 1.19 | 2.18 | 1.56 | 0.95 | 1.24 | |
![]() |
A | 0.33 | 2.74 | 3.96 | 0.33 | 2.40 | 1.22 | 0.95 | 1.17 | 0.89 |
| B | 0.64 | 1.22 | 4.19 | 0.64 | 0.58 | 2.97 | 0.72 | 1.74 | 0.65 | |
![]() |
A | 0.43 | 1.48 | 3.50 | 0.43 | 1.04 | 2.00 | 1.42 | 0.78 | 0.79 |
| B | 1.14 | 1.66 | 4.42 | 1.14 | 0.51 | 2.76 | 0.49 | 1.53 | 0.73 | |
| C | 0.62 | 1.54 | 3.84 | 0.62 | 0.91 | 2.27 | 1.10 | 1.04 | 0.60 | |
![]() |
A | 1.98 | 1.54 | 5.26 | 1.98 | –0.44 | 3.72 | –0.34 | 2.49 | 1.67 |
| B | 1.38 | 1.69 | 4.86 | 1.38 | 0.31 | 3.17 | 0.06 | 1.94 | 1.17 | |
| C | 1.68 | 1.87 | 5.00 | 1.68 | 0.20 | 3.13 | –0.08 | 1.90 | 1.31 | |
![]() |
A | –0.06 | 0.16 | 3.04 | –0.06 | 0.22 | 2.88 | 1.88 | 1.65 | 1.29 |
| B | 0.84 | 1.25 | 4.29 | 0.84 | 0.41 | 3.03 | 0.62 | 1.80 | 0.81 | |
![]() |
A | 1.72 | 1.78 | 4.89 | 1.72 | 0.06 | 3.11 | 0.03 | 1.88 | 1.20 |
| B | 1.50 | 1.47 | 4.82 | 1.50 | –0.04 | 3.35 | 0.10 | 2.12 | 1.27 | |
| C | 0.77 | 1.30 | 4.29 | 0.77 | 0.53 | 2.98 | 0.62 | 1.75 | 0.69 |
The detailed atomic structures are displayed in Figure S3.
The origin of reactive overpotentials
can be better understood
by plotting the free-energy diagrams, and the overpotentials strongly
depend on the free-energy difference between two reactive intermediates
of the RDSs. Figure 3b,c shows the OER free-energy diagrams on
and
at the equilibrium
potential (U = 1.23 V), respectively. By comparing
the free-energy diagrams at U = 1.23 V in Figures 1a,b and 3b,c, it is clearly
shown that the introduction of O atoms considerably tunes and enhances
the binding strength of reactive intermediates (O*, OH*, and OOH*)
with more negative adsorption energies. For the OER on
in Figure 3b, the RDS has translated to
the step of OOH* →
O2 (g) with a free-energy difference of 0.71 eV, corresponding
to the ηOER of 0.71 V. For
in Figure 3c, compared with pristine b-As
in Figure 1b, the step
of O* →
OOH* is still the OER RDS, while the free-energy gain has been reduced
to 0.94 eV, determining a better ηOER = 0.94 V.
Similarly, in Figure 4a, we summarize the ORR overpotentials ηORR’s
at different active sites on pristine and C- and O-doped b-As/g-As.
ORR overpotentials exhibit a similar volcano shape and can be tuned
within a wide range. Clearly, as denoted by the green circles, pristine
b-As and g-As locate at the bottom of the volcano shape, indicating
poor catalytic activity. For b-As, double O-doped
locates near the top
of the volcano peak
and exhibits the best ORR catalytic performance, with the lowest ηORR = 0.65 V. Among all O-doped g-As,
is the most effective
ORR catalytic structure,
with ηORR = 0.68 V. The corresponding ORR free-energy
diagrams on
and
are shown in Figure 4b,c, respectively.
The free-energy diagrams
in Figure 1 have shown
that the step of O2 → OOH* determines the ORR RDS
of pristine structures. In Figure 4b, the ORR RDS of
still originates from
O2 →
OOH*, but compared to over-high ηORR of 2.40 V on
pristine g-As, the ηORR has been significantly reduced
to 0.68 V due to the enhanced adsorption of OOH*. For
in Figure 4c, the ORR RDS has translated
to the step of O →
OH*, and excessive overpotential for pristine b-As (2.49 V) has been
optimized to 0.65 V.
Figure 4.
(a) Volcano plots for the ORR vs adsorption energies of
OH* on
single and double C and O-doped b-As and g-As. Free-energy diagrams
for the optimal ORR on (b)
and (c)
at U = 1.23 V. The corresponding
atomic structures of the adsorbed intermediate OOH* are shown in the
insets.
The improved OER/ORR activities of the above-mentioned O-doped configurations can be effectively attributed to the redistribution of surface charges induced by the introduction of O dopants into g- and b-As lattices. As shown in Figure S5, the distribution map of the charge density difference clearly demonstrates strong charge transfer between O atoms and the surrounding As atoms. Furthermore, Bader charge analysis shows that due to the larger electronegativity of O than As, the embedded O atoms attract more electrons with a negative Bader charge value, while the surrounding As atoms lose electrons and become positively charged. These As atoms with positive effective charges will facilitate the adsorption of reactive intermediates (O*, OH*, and OOH*) with negative charges and can act as potential active sites. As shown in Figure S6, the adsorbed intermediates usually obtain electrons from the catalyst surface and compared with the adsorption on the pristine surface, there is much more charge transfer from the O-doped surface to intermediates. Therefore, the resulting charge transfer has an effect on the ability of the adsorbed intermediates to obtain electrons from the catalyst surface, which is related to the adsorption strength of the intermediates, thus tuning the catalytic activity within a wide range.
Nowadays,
people are developing high-performance bifunctional catalysts,
which can catalyze the ORR and OER simultaneously.1,38 The
bifunctional catalytic performance could be well evaluated by calculating
the ORR/OER potential gap, that is, the sum of ηORR and ηOER.39,40 The lower ORR/OER potential
gap corresponds to a better bifunctional catalytic activity. Figure 3a shows that
exhibits the best
OER catalytic performance,
with ηOER = 0.71 V. Considering that the optimal
ORR activity with ηORR = 0.68 V, as shown in Figure 4a,
shows great potential
to act as an effective
bifunctional catalyst with a low ORR/OER potential gap of 1.39 V.
To better understand the overpotential origin, Figure 5a,b displays more detailed
free-energy diagrams for the optimal OER on
and ORR on
at different electrode
potentials, respectively.
In Figure 5a, for the
OER on
, when the
electrode potential U is 0 V, only the step of H2O → OH* is downhill
and other steps of OH* → O*, O* → OOH*, and OOH* →
O2 are uphill. As shown by the green lines, when U increases to the equilibrium potential 1.23 V, the free-energy
gains for the steps OH* → O*, O* → OOH*, and OOH* →
O2 have to be greatly reduced, but these three reactive
steps are still uphill, with the highest free-energy gain of 0.71
eV for OOH* → O2. Only when U increases
to 1.94 V shown by the blue lines, the free-energy gain of OOH* →
O2 could be reduced to zero and all reactive steps become
downhill, indicating that the OER reaction can occur spontaneously.
Therefore, ηOER is 1.94–1.23 = 0.71 V and
the RDS is the transformation from OOH* to O2. For the
ORR on
in Figure 5b, at U = 0 V, all steps are downhill.
However, when U increases to the equilibrium potential
1.23 V, three uphill steps appear and the transformation from O* to
OH* of the most endoergic step possesses the highest free-energy gain
of 0.65 eV. This free-energy gain will be reduced to zero only when U decreases to 0.58 V, corresponding to the ORR RDS of O*
→ OH*, with ηORR of 1.23–0.58 = 0.65
V. In addition, adsorbed intermediates O*, OH*, and OOH* on
and
are shown in each
diagram. The detailed
top and side views of atomic structures and charge density difference
of the adsorbed intermediates are displayed in Figure S6. It is clearly shown that the reactive active sites
in
and
locate at As sites
around embedded O atoms,
and strong charge transfer usually occur at adsorbed intermediates,
active sites, and neighboring As atoms.
Figure 5.
Free-energy diagrams
for the optimal (a) OER on
and (b) ORR on
at different electrode
potentials U. The
adsorbed intermediates O*, OH*, and OOH* on
and
are also shown. The
kinetic barriers for
(c) 2O* → O2 and (d) H2O → OH*
on
, and (e) O2 dissociation via
O2 → 2O* and (f) O2 → OOH* on
.
Through evaluating the kinetic barrier using the climbing image
nudged elastic band method,32,41 we further examine
the possibility of particular reactive steps, in which two adsorbed
O* species combine to form a O2 molecule (2O* →
O2) on
for the OER
and a O2 molecule
dissociates to two O* species (O2 → 2O*) on
for the ORR. For comparison,
we also examine
the kinetic feasibility of the OER and ORR initial reaction steps
of H2O → OH* on
and O2 →
OOH* on
, as shown
in Figure 5d,f, respectively. Figure 5c shows the reaction
progress of 2O* →
O2 on
, and it is
shown that the progress is endothermic
with a high energy barrier of ∼3.7 eV. This indicates that
during the OER on
, O* species
cannot directly coalesce to
produce O2 but must be assisted by the OOH* intermediate
group, as shown in Figure 5a. In contrast, in Figure 5d, the initial step of H2O → OH*
on
exhibits a lower energy
barrier of ∼1.32
eV, suggesting better OER kinetic feasibility. In Figure 5e, the energy barrier for the
dissociative O2 → 2O* pathway on
is as low as ∼0.48
eV with the exothermic
feature, indicating that this reaction pathway could easily occur
kinetically. In addition, from Figure 5f, it can be seen that the associative reaction step
of O2 → OOH* on
also possesses a low
barrier of ∼0.61
eV, and the exothermic feature indicates that this pathway is favored
energetically. Therefore, for the ORR on
, the O2 molecule may be able
to efficiently dissociate through dual reaction pathways: one is the
step-by-step reaction accompanied by the formation of the OOH* intermediate
(O2 → OOH* → 2O*), or the O2 molecule
dissociates directly into O* (O2 → 2O*). Such dual
reaction pathways will promote the ORR reaction rate on
.
Furthermore,
the influence of doping elements on HER catalytic
activity is also investigated. The HER catalytic performance can be
well characterized by the Gibbs free energy of H* adsorption (ΔGH*) on the reactive surface.42,43 The value of ΔGH* for an ideal
catalyst should be close to zero (ΔGH* ∼ 0). High ΔGH* will lead
to weak hydrogen adsorption on the catalyst surface, while low ΔGH* represents the strong binding of adsorbed
hydrogen and the surface, which will go against the dissociation of
the generated H2 molecule, both resulting in a slow HER
reaction. For better comparing the ΔGH* between different doping systems, we summarize the calculated ΔGH* at different reactive sites on
,
,
, and
in Figure 6a. It can be seen that embedded
heteroatoms can tune
ΔGH* within a wide range, especially
for C and O dopants. Among these doped configurations,
,
,
,
,
, and
can optimize ΔGH* to an appropriate value, which is close to zero and eligible
for HER catalysis, indicating improved reaction activity. Considering
the high formation energy of Sb dopants in Figure 2a, we only select C- and O-doped configurations
as effective HER catalysts, as labeled by black dotted rectangles
in Figure 6a. Figure 6b shows the HER free-energy
diagrams for pristine b-As/g-As,
,
,
,
, and
. As indicated by green
and red lines, pristine
b-As and g-As exhibit very weak hydrogen adsorption, with ΔGH* = 1.29 and 1.38 eV, which are not conducive
to the catalytic reaction and even prevents the reaction from occurring.
Clearly, embedding C and O dopants can provide sufficient adsorption
strength, especially for
with ΔGH* = 0.15 eV. The atomic structure of
with adsorbed H* is
displayed in the inset
of Figure 6b and the
active site arises from the embedded C atom. In Figure S5, the charge density difference and Bader charge
analysis clearly indicate that the enhanced HER activity mainly arises
from the strong charge transfer induced by the embedded O and C dopants,
which can effectively improve the adsorption strength of H*.
Figure 6.
(a) Calculated
ΔGH* for single-
and double-doped structures (
,
,
and
, X = C, O, P, S, and Sb).
(b) HER free-energy diagrams for b-As, g-As,
,
,
,
, and
. (c) Kinetic barriers
of the HER Tafel-step
reaction on
. (d) Atomic
structures of initial, final,
and intermediate NEB images.
For reducing protons to hydrogen in acid media, there exist two
different types of reaction pathways of the Volmer–Tafel and
Volmer–Heyrovsky mechanism.6 The
Volmer reaction is the first step in the HER process and refers to
forming adsorbed H* from the initial adsorption of proton in acid
solution. Based on the Volmer reaction, in the Volmer–Tafel
mechanism, two adjacent adsorbed H* species then react to form a H2 molecule (H* + H* → H2). However, in the
Volmer–Heyrovsky mechanism, adsorbed H* species reacts with
a proton accompanied by one electron to form a H2 molecule
(H* + H+ + e– → H2). Figure 6c presents the kinetic
progress of the HER on optimal
via the Tafel-step
reaction. The kinetic
barrier for this reaction is as high as ∼1.13 eV, comparable
to that of graphene(G)/MXene heterostructures (1.56 and 1.33 eV for
G/Mo2C and G/V2C, respectively)44 and MoS2 edges (1.0–1.5 eV),6 which will severely slow down the Tafel reaction.
However, the Heyrovsky-step reaction with a lower kinetic barrier
is usually much faster than the Tafel-step reaction.6 Therefore, the Volmer–Heyrovsky mechanism may be
the main reaction pathway of the HER on
.
Since the electrocatalytic
processes typically take place at the
solid–liquid interfaces,45 it is
very necessary to explore the influence of the solvent effect on catalytic
activities. As shown in Figures S7–S9, we adopted the simple explicit model to tackle solvent effects,
in which multiple water molecules are added on the catalyst surfaces
to model the aqueous interface. The atomic structures of intermediates
clearly indicate that there exists obvious hydrogen bonding between
adsorbates and water molecules, which could further stabilize the
adsorption of intermediates. As shown in Figures S7 and S8, the hydrogen bonding has different stabilizing effects
for intermediates O*, OH*, and OOH* on
and
, affecting the catalytic
performance to
some extent. For example, the calculated OER overpotential on
degenerates from 0.71
to 0.80 V at an aqueous
interface. For the HER process in Figure S9, it is clearly seen that the H* adsorption on
is further stabilized
by hydrogen bonding
with a lower ΔGH* value; hence,
the solvent effects give rise to a positive influence for the HER
activity on
. Therefore,
to more accurately describe
the catalytic characteristics of real solid–liquid systems,
solvent effects should be carefully considered in computational simulation.
As we know that electrical conductivity is a critical characteristic
quantity that determines the electron-transfer efficiency and catalytic
activity, which requires that the catalysts should be metallic or
semiconductors. Therefore, it is very necessary to characterize the
electrical conductivity properties of catalysts. Figure S10 shows the density of states of
,
, and
with optimal catalytic
activities. It can
be clearly seen that
and
demonstrate obvious
semiconductor properties,
and
exhibits favorable
metallicity, which indicates
that these explored surfaces possess good electrical conductivity
and can guarantee efficient electron transfer during catalytic reaction
progress. The calculated optimal overpotentials/ΔGH* and good electron-transfer characteristics together
prove the feasibility of our proposed effective catalysts.
Conclusions
In summary, using DFT calculations, we study the ORR, OER, and
HER catalytic activities of pristine and various heteroatom (O, C,
P, S, and Sb)-doped b-As/g-As. The results show that pristine b-As
and g-As exhibit poor catalytic performance for the ORR, OER, and
HER. Embedding heteroatoms can effectively tune the adsorption strength
of reactive intermediations and thus improve catalytic activities.
Compared with other candidate dopants (C, P, S, and Sb), O atoms are
more likely to be embedded into b-As and g-As lattices. More importantly,
O atom-modified b-As and g-As show superior catalytic properties for
the OER and ORR. For g-As, the OER and ORR catalytic activity can
be optimized simultaneously on single
, which exhibits great
potential as effective
bifunctional catalysts. However, the optimal OER and ORR catalytic
performance on b-As can be realized in
and
, respectively. NEB
calculations suggest
that
can achieve
the dual ORR reaction pathway
through O2 → OOH* → 2O* and O2 → 2O*. For the HER, C-doped
shows the best catalytic
performance, with
an appropriate ΔGH* of 0.15 eV,
and the Volmer–Heyrovsky mechanism is the main reaction pathway.
These findings would trigger more theoretical and experimental works
to further investigate the catalytic properties of As-based materials.
Acknowledgments
Y.F. is supported by the National Science Foundation of China (grant nos. 11604092 and 11634001) and the National Basic Research Programs of China (grant no. 2016YFA0300900). The computational resources were provided by the supercomputer TianHe-1 in Changsha, China.
Supporting Information Available
The Supporting Information is available free of charge at https://pubs.acs.org/doi/10.1021/acsomega.1c00908.
Further computational setups, detailed atomic structures of pristine black/gray arsenene and C- and O-doped configurations; scaling relationship between the adsorbed energies of reactive intermediates; and charge density difference for O*, OH*, and OOH* on
and
(PDF)
Author Contributions
# S.S. and P.S. contributed equally to this work.
The authors declare no competing financial interest.
Supplementary Material
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