Zhansheng Lua,
Peng Lva,
Jie Xuea,
Huanhuan Wanga,
Yizhe Wanga,
Yue Huanga,
Chaozheng He*b,
Dongwei Mac and
Zongxian Yang*ad
aCollege of Physics and Electronic Engineering, Henan Normal University, Xinxiang 453007, China. E-mail: yzx@henannu.edu.cn
bCollege of Physics and Electronic Engineering, Nanyang Normal University, Nanyang 473061, China. E-mail: hecz2013@nynu.edu.cn
cSchool of Physics, Anyang Normal University, Anyang 455000, China
dCollaborative Innovation Center of Nano Functional Materials and Applications, Henan Province, China
First published on 25th September 2015
Single metal atom catalysts exhibit extraordinary activity in a large number of reactions, and some two-dimensional materials (such as graphene and h-BN) are found to be prominent supports to stabilize single metal atoms. The CO oxidation reaction on single Pd atoms supported by two-dimensional h-BN is investigated systematically by using dispersion-corrected density functional theory study. The great stability of the h-BN supported single Pd atoms is revealed, and the single Pd atom prefers to reside at boron vacancies. Three proposed mechanisms (Eley–Rideal, Langmuir–Hinshelwood, and a “new” termolecular Eley–Rideal) of the CO oxidation were investigated, and two of them (the traditional Langmuir–Hinshelwood mechanism and the new termolecular Eley–Rideal mechanism) are found to have rather small reaction barriers of 0.66 and 0.39 eV for their rate-limiting steps, respectively, which suggests that the CO oxidation could proceed at low temperature on single Pd atom doped h-BN. The current study will help to understand the various mechanisms of the CO oxidation and shed light on the design of CO oxidation catalysts, especially based on the concept of single metal atoms.
Experimentally, there has been some progress on the concept of “single atom” catalysts (SAC) made through the use of mass-selected soft-landing technique, improved wet chemistry method, or atomic layer deposition methods to synthesize the single-atom species on various supports.6–8 The stability of the single atom catalysts is a crucial challenge due to the mobility of single atoms.9 A practical Pt single atom catalyst supported by iron oxide was experimentally prepared for the first time by Qiao et al. (denoted Pt1/FeOx), and the excellent performance of Pt1/FeOx demonstrates that heterogeneous catalysis with single atom catalysts is no longer an unattainable goal.10 Moreover, two-dimensional (2D) materials with large specific surface area and great stability, such as graphene, and freestanding hexagonal BN monolayers (h-BN), are found to be prominent catalyst supports to stabilize single metal atoms. For example, single atomic Au on h-BN with boron vacancies exhibits great thermal stability even during the CO oxidation process,11 while single Ru atoms embedded on h-BN are extraordinarily stable because of their dramatically huge diffusion energy barrier.12
Graphene supported individual, isolated Fe,13 Au,14 Pt15,16 and Cu17 atoms present great activity and selectivity to the CO oxidation reaction and h-BN supported single atomic Au,11 Ru,12 Co,18 Cu,19 Pt20 and Fe21 promote CO oxidation at the low temperature. Pd and its alloys, as typical catalysts for CO oxidation, present high activity.22,23
In the current study, considering the joint system of Pd and 2D freestanding material, we focus on the stability and activity of the single atomic Pd supported by h-BN (Pd1-BN) for CO oxidation. The stability of Pd1-BN will be revealed by the mobility of the single Pd adatom from the calculated diffusion barrier. The entire CO oxidation process on Pd1-BN is investigated with various adsorption configurations of CO and O2 and the different reaction mechanisms of CO oxidation, via a new mechanism over the normal bi-molecule Eley–Rideal (ER) and Langmuir–Hinshelwood (LH) mechanisms. Whether and how single Pd atoms could promote the CO oxidation will be focused on. The current study will help to understand the various mechanisms of CO oxidation and shed light on the design of the CO oxidation catalyst based on the single metal atom concept, and various catalysts for other reactions based on the single metal atom concept.
The calculated lattice constant of h-BN is 2.51 Å with the B–N bond of 1.45 Å, which is in good agreement with the previous study.21 The BN support is modeled by a 4 × 4 h-BN supercell with a vacuum layer of 15 Å. The test calculations suggest that the current model is suitable to reveal the CO oxidation process. The adsorption energy (Eads) is defined as Eads = Eadsorbate + Esupport − Eadsorbate/support, where Eadsorbate, Esupport and Eadsorbate/support are the total energies of the free adsorbate, the corresponding support and the support with the adsorbate, respectively. All three types of energy were derived from the calculations using the same periodic box dimensions and the same calculated setting. With this definition, a positive value indicates an exothermic adsorption.
For the defect h-BN, we consider both the N-defect and B-defect h-BN as supports to anchor single Pd atoms from the various initial structures.28 Their most stable configurations are presented in Fig. 1c and d, and marked as Pd1-NV/BN and Pd1-BV/BN, respectively. Upon binding on the defect-BN, the formed Pd–B and Pd–N bonds secure the single Pd atom with bond lengths of 2.04 and 1.98 Å, respectively. The corresponding adsorption energies are 4.51 and 5.33 eV, respectively, both of which are larger than the binding energy of Pd dimer (1.19 eV) and Pd bulk (3.89 eV). This indicates that both defect-BN configurations provide stable anchoring sites for the single Pd atoms. The B-defect is more strongly binding than the N-defect in BN, according to the calculated formation energies29 and fortuitously boron mono-vacancies are preferably fabricated experimentally by high energy charged electrons.30 Thus, the Pd1-BV/BN configuration would be more preferable than the Pd1-NV/BN configuration, and the former will be focused on in the following.
To gain a deeper insight into the properties of the Pd1-BV/BN configuration, we perform the electronic structure analysis of the partial density of states (PDOS) and the Mulliken charge population analysis. The DOS curves are presented in Fig. 1e, and there are many overlapped peaks between the Pd-4d states and the N-2p states, indicating the hybridization between Pd-4d states and N-2p states, resulting in the strong interaction of the Pd and its three neighbor N atoms. Moreover, there are four sharp peaks (two from Pd-4d states and the other two from N-2p states) across the Fermi level (EF), suggesting the high activity of the Pd1-BV/BN system. As indicated by the charge density difference (Fig. 1f), there is charge transfer from the Pd atom to the BV/BN support, and the transferred charge is mainly localized on the three neighboring N atoms of the Pd adatom. The Mulliken charge analysis shows the charge transfer from Pd atom to BV/BN support is 0.19|e|.
As a catalyst, the stability of single atomic Pd adsorbed on BV/BN is highly important. Here, we investigate the mobility of the single Pd atom to reveal the stability of the Pd1-BV/BN system, and we take the most stable adsorption site as the initial state (IS), and the other two stable ones as the final states (FS1 and FS2, respectively). The calculated mobility barrier of the Pd atom from IS to FS1 and FS2 are 3.77 and 5.26 eV, respectively (see Fig. 2). The large diffusion barriers indicate the immobility of the single Pd atom on the B-defect h-BN. The immobility of the single Pd atom together with its strong adsorption energy (compared to the binding energy of Pd dimer and bulk) implies that the metal clustering of Pd atom would be rather difficult and the Pd1-BV/BN configuration is extraordinarily stable, which might allow higher temperature conditions of operation.
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Fig. 2 The reaction profiles of diffusion of single Pd atom from its most stable adsorption site to the other stable adsorption sites. |
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Fig. 3 Top and side views of the most stable adsorption configurations of (a) O2, (b) CO, (c) O and (d) CO2 on Pd1-BV/BN. Hereafter, the red and gray spheres represent O and C atoms, respectively. |
The adsorbed O2 molecule anchors on the Pd adatom and prefers to lie parallel to the h-BN support, and the O–O bond is enlarged from 1.23 to 1.33 Å with two Pd–O bonds of 2.12 Å being formed, and the calculated adsorption energy is 1.01 eV. According to the Mulliken charge analysis, the adsorbed O2 is negatively charged by 0.34|e|, and the single Pd adatom is positively charged by 0.28|e|, indicating the key role of the Pd atom to activating the adsorbed O2. Fig. 4 presents the PDOS curves of the related systems of O2 and CO adsorption on Pd1-BV/BN. Upon O2 adsorption, the curve of Pd-4d states is broadened, and there are two new hole peaks appearing above the Fermi level to overlap with the 2π* orbitals of O2. At the energy region of −7.5 to −5.0 eV, there are three peaks of the 1π orbitals of adsorbed O2, and the three peaks well overlap with the three peaks of the Pd-4d states, implying the strong hybridization between the Pd-4d states and the 2p states of the adsorbed O2. The elongation of the O–O bond, the substantial charge transfer and the strong hybridization of the Pd-4d states and O-2p states suggest that the O2 is significantly activated.
The most stable CO adsorption configuration is presented in Fig. 3b and the CO is tilted to the Pd1-BV/BN plane with a C–O bond of 1.15 Å (similar to gaseous CO), and C–Pd bond of 1.91 Å. The calculated adsorption energy is 1.07 eV, which is only 0.06 eV more favorable than that for O2 adsorption, suggesting that the adsorption of CO is slightly preferred. The Mulliken charge analysis shows that the adsorbed CO is positively charged by 0.26|e| and the Pd accepts 0.25|e| while the changes of boron and nitride atoms charges are negligible, indicating the CO and the Pd act as a charge donor and acceptor, respectively. As shown in Fig. 4b, upon CO adsorption, the Pd-4d states split into two peaks near the Fermi level, and the two peaks strongly hybridize with the 2π* orbitals of the absorbed CO. In the energy area of −12 to −7 eV, the 4σ and 1π orbitals of CO are also hybridized with the Pd-4d states. The strong hybridization between CO and Pd is in line with the strong interaction between Pd and CO.
The most stable adsorption structure of a single O atom on Pd1-BV/BN is presented in Fig. 3c. Compared with that of O2 adsorption (Fig. 3a), the adsorption energy of the O atom is reduced to 0.34 eV and the O–Pd bond is reduced to 1.81 Å. The adsorbed O atom is negatively charged by 0.48|e| [about half of q(O2−)],31 indicating the formation of the O− species. The O− species is believed to be more reactive than O2−.32 As presented below, the O− species shows high activity to oxidize the CO.
As the final product of CO oxidation, only the physical adsorption configuration is found for the CO2 adsorption (Fig. 3d), with a rather small adsorption energy of 0.06 eV and a long Pd–O distance of 2.93 Å. The rather weak interaction (the small adsorption energy) together with the negligible charge transfer between the CO2 and support indicates that the formed CO2 species would be spontaneously released at room temperature.
Interestingly, two new CO oxidation mechanisms have been proposed, denoted as termolecular Eley–Rideal mechanism (TER) by Yang et al.11 and termolecular Langmuir–Hinshelwood mechanism (TLH) by Zeng et al.34 In the TER mechanism, a free O2 molecule is activated by two co-adsorbed CO molecules to form an OCO–metal–OCO intermediate, which is a pentagonal ring structure, and the intermediate configuration would dissociate into two CO2 molecules synchronously. In the TLH mechanism, the initial state is the configuration whereby one O2 molecule and two CO molecules are co-adsorbed on catalyst. The presence of the OCOPdOCO intermediate and the co-adsorption configuration of two CO molecules (as presented below) on the Pd1-BV/BN support implies the probability of the TER mechanism for CO oxidation. However, the absence of the co-adsorption configuration of one O2 and two CO molecules suggests that the TLH mechanism is not applicable for CO oxidation on the Pd1-BV/BN system. Furthermore, the co-adsorption configuration of three CO molecules is also taken into consideration, and it is found that the Pd1-BV/BN is unable to chemisorb a third CO, which avoids the CO poisoning problem20 and leaves the possibility of CO oxidation through the ER, LH and TER mechanisms.
Given that the adsorption energies of CO and O2 are both lower (∼0.2 eV) than the reaction barrier of the formation of the carbonate-like structure, the desorption of adsorbed CO and O2 would be slightly preferable relative to the formation of the carbonate-like structure. This indicates that the CO oxidation over Pd1-BV/BN via the ER mechanism is not preferable, which is similar to that of CO oxidation on Cu embedded in h-BN via the ER mechanism.19 Therefore, the LH and TER mechanism will be emphasized in the following. The oxidation of the second CO by the remaining atomic O on Pd1-BV/BN will be presented in the next subsection.
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Fig. 6 The reaction profiles of CO oxidation via the LH mechanism. The two O atoms of the O2 molecule are labelled as O1 and O2, respectively. |
Upon the cleavage of the O–O bond of the oxygen molecule a CO2 molecule is formed, and the corresponding reaction energy barrier and exothermic reaction energy is 0.61 and 2.11 eV, respectively. Similarly, due to its rather weak adsorption and the long distance to the support, the formed CO2 will be spontaneously released as free CO2 at room temperature.
Upon the release of the formed CO2, there is an atomic O left on the Pd1-BV/BN with a Pd–O bond of 1.81 Å. It is found that this atomic O is negatively charged by 0.48|e| [about half of q(O2−)], implying the formation of the O− species.31 The O− species is believed to be more reactive than O2−,32 and will readily oxidize a second CO. The 2nd CO is first physically adsorbed at the atomic O with a C–O distance of 3.03 Å. When the CO approaches the atomic O to form the second CO2 molecule the reaction energy barrier and exothermic reaction energy are 0.23 eV and 2.94 eV, respectively. The adsorption of the formed CO2 is rather weak (0.06 eV), suggesting that the formed CO2 species would be released spontaneously and Pd1-BV/BN system is renewed and ready for a new cycle of CO oxidation.
To summarise, the corresponding rate-limiting step is TS2 (0.66 eV) with the formation of the OCOO intermediate, which is endothermic (0.13 eV). In the LH mechanism, the reaction energy of the entire reaction process from the co-adsorption of O2 and CO to the formation of the first CO2 is exothermic (2.37 eV), and it can compensate for the small endothermic reaction energy of the rate-limiting step (0.13 eV). In addition, the final product in FS2, CO2, shows weak adsorption on Pd1-BV/BN catalyst and it will be easily desorbed, suggesting the concentration of reactants (CO and O2) is higher on the catalyst than the product (CO2). All these results indicate that the CO oxidation reaction via the LH mechanism is hardly inhibited by the step from MS1 to MS2 and the chemical equilibrium will shift to the formation of the product CO2.
For the configuration of two CO molecules co-adsorbed on Pd1-BV/BN, the adsorption energy of the second CO is 0.77 eV and the co-adsorption energy is 1.84 eV. In the reported TER mechanism of the CO oxidation on the Au–BN system, the two adsorbed CO molecules would promote the activation of the O2 molecule, i.e. the O2 molecule is activated by CO molecules directly.11 Indeed, we also found the activation of the O2 is promoted by the two pre-adsorbed CO molecules on the Pd1-BV/BN. In the initial state, two CO molecules are chemically co-adsorbed on a Pd atom with one physically adsorbed O2 molecule, where the distances of O1–C1 and O2–C2 are 3.46 and 3.78 Å, respectively, and the angle of C1–Pd–C2 is 95.08°. The physically adsorbed O2 molecule first approaches the two carbon atoms simultaneously via a rather small reaction energy barrier of 0.03 eV to form the OCOPdOCO intermediate, and the corresponding (exothermic) reaction energy is 1.23 eV. The formed OCOPdOCO intermediate has a pentagonal ring structure (see the “MS” of Fig. 7), in which the O–O bond is enlarged to 1.49 Å. Subsequently, the OCOPdOCO intermediate dissociates to form two adsorbed CO2 molecules with the cleavage of the O–O bond via TS2, and the corresponding reaction energy barrier and (exothermic) reaction energy are 0.39 and 4.32 eV, respectively. Moreover, the adsorption energies of the formed CO2 molecules are rather small (∼0.16 eV), suggesting that the formed CO2 molecules would be released spontaneously and the Pd1-BV/BN system is renewed and ready for a new cycle of CO oxidation.
To summarise, in the current TER mechanism, the rate-limiting step is the formation of the two CO2 molecules from the dissociation of the OCOPdOCO intermediate with a small reaction energy barrier of 0.39 eV. This suggests high activity of the Pd1-BV/BN for CO oxidation, which is mainly attributed to the “CO-promoted O2 activation”.11 The positively charged carbon atoms of the CO molecules would be a good anchor for the negatively charged O2. The energy barrier of the rate-limiting step for TER is dramatically lower than that for LH mechanism (0.39 vs. 0.66 eV), indicating that the TER mechanism (CO-promoted O2 activation) would be more preferable than the LH mechanism. According to the initial stage of LH (CO and O2) and TER mechanism (2CO), when first loading one reactant (O2) at a time, beginning with the co-adsorption of O2 and CO followed by the formation of OCOO intermediate, the LH mechanism will take place. On the contrary, when first loading another reactant (CO) at a time, beginning with the co-adsorption of two CO followed by the formation of OCOPdOCO intermediate, the TER mechanism will take place. However, it is quite impractical to feed the two reactants sequentially. In order to improve the reaction activity by the most preferable mechanism (TER), the concentration of the CO should dominate over that of O2 in the mixed feed. In order to improve the reaction activity by the most preferable mechanism (TER), the concentration of the CO should dominate over the O2 in their mixed feed. CO will firstly occupy the Pd site and be oxidized by the activated O2 via the most preferable TER mechanism, which also shrinks the possibility of the co-adsorption of CO and O2 on Pd1-BV/BN, i.e. the LH mechanism.
Summarizing our calculated reaction energy barriers for all of the CO oxidation mechanisms (ER, LH, TER), it is concluded that the traditional mechanism (LH) and the new mechanism (TER) are both preferable for CO oxidation on Pd1-BV/BN under experimental conditions because of the high reaction energy barrier of the rate-limiting step in ER mechanism. The rate-limiting steps for the preferable LH and TER mechanisms are the formation of the OCOO intermediate and the formation of the two CO2 molecules from the dissociation of the OCOPdOCO intermediate, respectively, and the corresponding reaction barriers of the rate-limiting steps for the two mechanisms are 0.66 and 0.39 eV, respectively. Given the relatively small energy barriers for LH and TER (0.66 and 0.39 eV, respectively), we believe that both two mechanisms are possible and could occur at low temperature. Also, the energy barrier of the rate-limiting step for TER is dramatically lower than that for LH mechanism (0.39 vs. 0.66 eV), indicating that the TER mechanism (CO-promoted O2 activation) would be more preferable than the LH mechanism.
Utilization of the novel properties of SACs seems to provide vast opportunities for their applications in heterogeneous catalysis. The current study will help to understand the various mechanisms of the CO oxidation and shed light on the design of CO oxidation catalysts based on the single metal atom concept, to lower CO emissions, and solve the growing environmental problem. With the establishment of SACs as a new concept and a thorough elucidation of the nature of single atom catalysis, we believe that the development and understanding of SACs might be a new frontier in heterogeneous catalysis.
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