DOI:
10.1039/C9RA02172H
(Paper)
RSC Adv., 2019,
9, 21626-21636
CO oxidization catalyzed by B, N, and their co-doped fullerenes: a first-principles investigation†
Received
20th March 2019
, Accepted 2nd July 2019
First published on 12th July 2019
Abstract
Using the elastic band method based on first-principles calculations, we have carefully studied the catalytic properties of B, N, and their co-doped fullerenes. During oxidization of CO, both C59B and C59N can be oxidized to form durable oxide catalysts for successive CO oxidizations, the rate determining steps of which have 0.59 and 0.80 eV barriers, respectively. In CO-rich conditions, the C59N may remain in the entire reaction cycle with a 0.44 eV rate determining barrier. Both BN-pair doped fullerene and B-rich B3N doped fullerene can also be oxidized during the process of catalyzing CO oxidizations, and the oxides can then be repeatedly used as catalysts in successive CO oxidizations with rate determining barriers of approximately 0.42 eV. The central B in the N-rich C56BN3 is protected by its surrounding N atoms against oxidization to remain as a durable catalyst, the rate determining barrier of which is 0.63 eV for catalyzing CO oxidization. These results for the B and N doped fullerenes, and especially for the B–N co-doped fullerenes, could help in the design of high-performance non-metal catalysts, calling for further detailed experimental investigations.
1. Introduction
The increased energy demand and the corresponding rapid consumption of various fuels have attracted extraordinary research interests that are focused on environmental pollutants. Among these CO has been identified as a poisonous pollutant species and has already aroused intensive research attention during the past few decades. It is usually generated by incomplete combustion of various fossil energy sources, for example emissions from vehicle exhaust fumes, various industrial processes, the consumption of fossil energy materials, and so forth. It can bind to hemoglobin more strongly than O2 to reduce oxygen availability for different organs, resulting in impaired concentration, slow reflexes, and confusion. In addition, CO in fuel cells is a critical and harmful issue, especially with regard to the large-scale application of fuel cells as sustainable energy carriers, which could poison the electrode making it inactive. With regard to cleaning, effective heterogeneous catalysts for CO oxidization play a critical role. Usually, precious metals or their related alloys or oxides are needed for catalysis of the CO oxidization reaction, for example Pt, Au, Ru, Rh, and Pd.1–23 However, these metal catalysts are expensive and usually need to be used at a high temperature to achieve an efficient operation. Finding inexpensive alternatives to replace these precious metal-based catalysts is therefore highly desirable. Therefore, investigation of low-priced metal-free catalysts has gained tremendous research interest in recent decades.
Recently, carbon or carbon-based nanomaterials have been found to have superior catalytic properties, and a significant amount of research has been focused on exploring non-metal catalysts. These carbon nanomaterials, which have sp2-like hybridization networks including graphene, nanotubes, fullerene, and so forth, have abundant free-flowing π electrons to provide reactions requiring electrons, and this makes them potential base materials for exploring high-performance metal-free catalysts. However, the π electrons in ideal sp2-like nanostructures, such as C60, are too inert to be directly used to catalyze reactions. In recent years, studies have shown that breaking the integrity of the π electron distribution in heteroatom doped sp2-like nanostructures could activate π electrons, giving them superior catalytic properties.24–27 Owing to the difference in the number of valence electrons, B and N are the most frequently studied heteroatom doping species. The doped C60 structures with a maximum number of doped B and N were previously studied by Manaa et al.28–30 N doping can cause conjugation of the lone-pair electrons with the carbon π electrons to allow the surrounding C atoms to become active for O2 adsorption. In contrast, the doping of the electron deficient B atom in carbon networks can only provide a vacant 2pz orbital for conjugation with carbon π electrons, resulting in B becoming an active site for O2 adsorption. Hu et al.31 and Lin et al.32 studied the CO oxidizations catalyzed by N doped carbon nanotubes using density functional theory (DFT) calculations. Chen and his co-workers reported DFT studies on CO oxidizations catalyzed by N doped C60 (ref. 33) and penta-graphene.34 In addition, B, N, P, and Si-doped graphene also shows superior reactivities for catalyzing CO oxidizations.35–39 Despite the great progress that has been made in the search for heteroatom doped carbon nanostructure catalysts, studies providing detailed reaction paths are still highly desired to give deeper insights into the catalytic origin, aiming to help researchers design high-performance and durable metal free catalysts. To the best of our knowledge, comparative theoretical studies on the catalytic properties of B, N and their co-doped C60 are limited and there are no detailed studies on the catalytic properties of the corresponding oxides of doped C60, which are the by-products of the pioneering CO oxidizations.
In this paper, by using B or N doped C60, and their co-doped fullerenes as prototype nanostructure catalysts, we carefully studied the minimum energy reaction paths of CO oxidizations by using the elastic band method based on first-principles calculations. Our studies suggest that the carbon-based nanostructures would experience oxidization during catalyzing CO oxidizations. The catalytic properties of these oxides are investigated for the first time, as these could then act as durable recycling high-performance catalyst species for successive CO oxidization cycles. Furthermore, our studies on the BN-pair, BN3, and B3N doped C60 could shed light on the development of metal-free catalysts by using small B–N co-doping motifs, either in stoichiometric or B- and N-rich conditions.
2. Computational details
We have carried out detailed minimum energy reaction path studies based on first-principles calculations which were performed within the framework of spin-polarized DFT as implemented in the Vienna ab initio simulation package (VASP).40 The projector augmented-wave method was employed and a cutoff energy of 400 eV was used for the plane wave bases to construct the wave functions.41 The exchange–correlation energy was calculated by using generalized gradient approximation (GGA) with the Perdew, Burke, and Ernzerhof (PBE) parameterized functional.42 In order to mimic the zero-dimensional materials, a supercell with a vacuum space of more than 10 Å was employed to clearly separate the cluster and its periodic images in order to eliminate the interaction between them. For such a large supercell, only the Γ point was used to integrate the electronic properties in the first Brillouin zone. The convergence criterion of the electronic properties was set to 10−5 eV. The positions of the atoms were fully optimized until the maximum force acting on each atom converged to 0.01 eV Å−1. For the minimum energy path, we first carried out a 16-image nudged elastic band method (NEB) calculation. Based on the optimized NEB path, we re-optimized the reaction path by using the elastic band method with a dense image set around the saddle point along the reaction path, with the purpose of obtaining a sense of the accurate energy barrier.43–45 Along the entire reaction cycle, we compared the calculated barriers and chose the largest one as the rate determining barrier. The adsorption energy was calculated by referring to the free-standing gas molecule and nanostructure:
Eads = Efullerene+molecule − Efullerene − Emolecule |
In which Efullerene+molecule, Efullerene, and Emolecule were the total energies of the molecule adsorbed structure, the doped fullerene, and the isolated molecule, respectively. A negative value indicates an exothermic process. In addition, we also calculated the frequencies of the initial, transition, and final states of all of the studied reaction paths. The vibration properties were studied by using the linear response method as implemented in the VASP code.
3. Results and discussion
3.1 Catalytic properties of B and N doped fullerenes
3.1.1 Gas molecule adsorption on C59B and C59N. We started our studies by considering the adsorptions of O2 and CO small gas molecules on the singly doped fullerenes. Firstly, we calculated the formation energy of the doped structure using:
In which EC60−nXn is the total energy of the doped configuration. X represents B or N. μC and μX are the chemical potentials of C in graphene and X in its bulk. Although C60, C59B, and C59N were calculated to have formation energies of 0.373, 0.387, and 0.380 eV, they have previously been fabricated in experiments. In order to estimate their stabilities, we performed first-principles molecular dynamics simulations (FPMD) at 1000 K, which last for 5 ps with a time step of 1 fs. The geometrical structures are found to be retained during our FPMD studies, suggesting their stability. Once they were formed in the experiments, they could be then used as catalysts for CO oxidization. Both CO and O2 could be exothermically adsorbed onto C59B, the lowest energy adsorption configurations for which are shown in Fig. 1a and b, respectively. The corresponding adsorption energies are −0.80 and −1.02 eV. Our elastic band method studies show that CO adsorption is barrierless. The reaction energy, such as the energy barrier, is defined as:
Ereaction = Einter − Einitial |
|
| Fig. 1 The structures of CO adsorption (a), O2 adsorption (b) and (c), and CO and O2 co-adsorption (e) and (f) on C59B. (d) The lowest energy structure of O2 molecules on C59N. The adsorption energies are also given. (g) and (h) Show the reaction paths for CO oxidization catalyzed by C59B. The initial, final, saddle, and meta-stable intermediate states are illustrated in the inset figures. C, B, N, and O are represented by the grey, pink, blue, and red balls. | |
In which the Einter and Einitial are the calculated total energies of the intermediate state along the reaction path and the initial reaction state, respectively. A positive value indicates there is an energy cost to activate the reaction. However, the O2 must first overcome the 0.06 eV energy barrier to cap onto the B atom in an end-on adsorption configuration (see Fig. 1c), then reach the final chemisorption state by overcoming a 0.05 eV energy barrier. In the final adsorption state, the O atoms connect with the B and its adjunct C atoms. The O–O bond is roughly parallel to the B–C bond below. The bonding between O and C59B results in a charge transfer of approximately 0.86e (calculated using the Bader analysis technique46) from C59B to O2 to elongate the O–O bond by 0.19 Å to activate the O2, which is close to previously reported results.33,47–49 In our calculation, the O2 is found in the 3Σg− triplet ground state before adsorption onto C59B. When it gets close enough to C59B to adsorb onto it, a charge transfer would occur. In the final adsorption state, the charge gain elongates the O–O bond and transfers it into the 1Δg singlet excited state. In contrast to the gas adsorption on C59B, the C59N can only adsorb O2, for which our elastic band method calculations did not find a barrier. The adsorption energy was calculated to be −0.29 eV. The O2 could only be adsorbed in an end-on adsorption configuration as shown in Fig. 1d with one of its O atoms being connected to the adjacent C atom around the N dopant, gaining approximately a 0.36e charge to elongate the O–O bond by 0.06 Å. The O2 is then transferred from the 3Σg− triplet ground state to the 1Δg singlet excited state.
3.1.2 Catalytic properties of C59B and its oxide. In order to examine the catalytic properties of the singly doped fullerene, we studied the oxidization reaction of the CO molecule. As both the O2 and CO could be absorbed onto C59B, we started our studies from their co-adsorption configuration. The optimized co-adsorption configurations are shown in Fig. 1e and f. The configuration in Fig. 1e represents the adsorption process of the O2 approaching C59B first, and Fig. 1f shows the process with CO adsorption being followed by an O2 molecule approaching. According to our calculations, the configuration in Fig. 1e is approximately 0.12 eV lower in total energy. Starting from the lowest energy co-adsorption configuration, we carefully studied the CO oxidization reaction path, which is shown in Fig. 1g. We have also calculated the frequencies of the stationary point structures during the reaction, the results are shown in Fig. S3 in the ESI.† The frequencies of the reactants and products are positive, while the transition states have only one imaginary mode. An energy of 0.48 eV could activate the reaction. As shown in the inset image showing the structure of saddle point B in Fig. 1g, the reaction would start with the dissociation of an O2 molecule to provide an atomic O for CO oxidation through the Eley–Rideal (ER) mechanism, which then moves into a meta-stable state. One of the dissociated O atoms connects with the B atom and its nearest C atom to oxidize the C59B. Another O atom connects with B and the C of the CO molecule simultaneously, forming a complex O–C–O species. Then, an activation energy of 0.44 eV could desorb the O–C–O to release an CO2 molecule. Referring to the whole reaction path, we conclude that the energy barrier is about 0.48 eV and this was used to determine the reaction rate for this reaction, as shown in Fig. 1g.The reaction product C59BO, as shown in Fig. 2a, could be further used as a catalyst. First, we consider the case of a CO molecule approaching the O atom in the C59BO oxide, which was found to have an energy barrier of approximately 1.47 eV in the converged reaction path shown in Fig. 1h, this limits its occurrence. Interestingly, the B atom in C59BO oxide is still able to bond an O2 molecule. There is only a 0.02 eV energy barrier for O2 adsorption, which forms a 1.54 Å BO bond in the end-on adsorption configuration shown in Fig. 2b, the adsorption energy is −0.76 eV. The O–O bond was found to be elongated by 0.08 Å. A charge gain of approximately 0.64e was confirmed by our Bader charge analysis for O2, which helps to transfer it from a 3Σg− triplet state to a 1Δg singlet state. As shown in Fig. 2g, a CO could approach the adsorbed O2 to form the O–O–C–O complex species through the Langmuir–Hinshelwood (LH) oxidization mechanism by overcoming the 0.63 eV energy barrier, which would evolve to release a CO2 molecule under a 0.21 eV activation energy, leaving a single O atom adsorbed on the B atom. Providing that it is used in the CO-rich surrounding conditions, the produced atomic O could be removed from the C59BO oxide through oxidization of one more of the CO molecules (the barrier is 0.11 eV). Otherwise, it would directly react with the doped fullerene to form C59BO2 oxide (see the structures shown in Fig. 2c), which require a 0.17 eV activation energy. It should be mentioned here that the C59BO2 oxide could also be obtained from the lowest energy chemisorption state of O2 on C59B under a 0.24 eV activation energy for O2 dissociation and then after the oxidization process. After this, one more O2 could rapidly be attached onto the C59BO2 oxide (see Fig. 2d for adsorption configuration), which could then be used to oxidize one more CO under a 0.37 eV activation energy along the converged pathway presented in Fig. 2h to produce a CO2 molecule and an atomic O. For the O2 adsorption on the C59BO2 oxide, a charge of approximately 0.70e is transferred from the oxide to the O2 molecule, making the triplet-singlet state transition which elongates the O–O bond by 0.10 Å. The produced atomic O would either oxidize one more CO or directly react with C59BO2, depending on whether it is protected by CO molecules or not. The oxidization of CO requires an activation of 0.11 eV, while the barrier is 0.09 eV for the oxidization of C59BO2 to form C59BO3 oxide (see Fig. 2e for the geometrical configuration). Again, an O2 molecule could be adsorbed onto the B atom through an exothermal adsorption process, forming a 1.23 eV lower end-on chemisorption state, which is also transferred into the 1Δg singlet excited state by gaining a ∼0.73e charge. Correspondingly, the O–O is elongated by 0.10 Å. As shown in Fig. 2i and j, the C59BO3 oxide could be repeatedly used as a catalyst for CO oxidization. Therefore, in the process of CO oxidization on C59B, the doped fullerene would have the chance to change to the new catalyst species, C59BO3 oxide. The corresponding rate determining barrier is only 0.59 eV for the CO oxidization cycles catalyzed by C59BO3 oxide, showing a good catalytic performance. In addition, we have also calculated the CO adsorption on nicked C59BOx (x = 1–3) oxides, which are only weakly adsorbed and could be easily removed from the C59BOx oxides to leave the B atom for O2 adsorption. The superior catalytic properties of the C59BOx oxides are mainly associated with the activation of the adsorbed O2. In addition, in Fig. 2k and l, we present the optimized reaction pathway starting from another CO–O2 co-adsorption state as shown Fig. 1f. The CO would be oxidized by the LH oxidization mechanism releasing an CO2 molecule and producing the C59BO oxide, for which the higher energy barrier is 0.51 eV. Again, the produced C59BO oxide could be further used to catalyze CO oxidizations through the reactions studied in Fig. 2g–j to finally obtain the C59BO3 oxide. Also, for the C59B oxide materials, we have carried out FPMD simulations. The C59BO, C59BO2, and C59BO3 were found to be well preserved in our 5 ps simulations at 1000 K, suggesting their stabilities.
|
| Fig. 2 (a)–(f) Show the structural skeleton illustrations for C59BO, C59BO2, C59BO3 oxides, and the O2 molecule adsorption configurations on the different oxide structures of C59B, respectively. (g)–(l) Show the reaction paths for CO oxidization on C59B oxide catalysts. The initial, final, saddle, and meta-stable intermediate states are illustrated by the inset images. C, B, and O are represented by the grey, pink, and red balls. | |
3.1.3 Catalytic properties of C59N and its oxide. Unlike C59B, C59N could only chemically adsorb O2. The adsorption process is barrierless and the stable state is a 0.29 eV lower end-on configuration. Our Bader charge analysis shows approximately a 0.37e charge transfer from C59N to O2, transferring it from the 3Σg− triplet ground state to the 1Δg singlet excited state. The O–O bond was found to be elongated by 0.07 Å. On C59B, the best adsorption site for O2 is on top of the B dopant. However, the N dopant in C59N is not the active site, however, this makes the surrounding C atoms active. Our calculations show that the adsorption of O2 would only develop an O–C bond with the nearest C atom. The lowest chemisorption adsorption state of O2 on C59B with O–O being parallel to the B–C bond is not stable in the case of O2 adsorption on C59N. The adsorption of O2 on C59N increases the O–O bond length by 0.06 Å. An incoming CO molecule could be oxidized by overcoming the 0.44 eV energy barrier (see Fig. 3d). The produced single O atom could be easily removed by one more CO providing that it is in the CO-rich surrounding conditions to provide sufficient CO molecules around the catalyst. Otherwise, this O would directly react with fullerene to form the C59NO oxide by overcoming a 0.20 eV energy barrier, which is found to have a good stability using our FPMD simulations performed for 5 ps at 1000 K. The geometrical structures of the C59NO oxide and the corresponding chemisorption state of a O2 molecule upon it are shown in Fig. 3a and b, respectively. The adsorption of O2 onto the C59NO oxide gains approximately a 0.45e charge to elongate the O–O bond by 0.10 Å to reach the 1Δg singlet excited state. In Fig. 3e and f, we studied the catalytic performance of the C59NO oxide for CO oxidization. The rate determining barrier was found to be 0.80 eV. In contrast to that observed for the B doped fullerene, the C59NO oxide species would repeatedly act as a oxide catalyst in the successive CO oxidization cycles. The atomic O produced in the reaction shown in Fig. 3e does not like to move to the bridge sites to form two bonds with fullerene simultaneously (see Fig. 3c), and would therefore remain to catalyze another CO molecule through the reaction shown in Fig. 3f to produce CO2 and C59NO oxide.
|
| Fig. 3 (a) Structural skeleton illustrations for the C59NO oxide; and (b) the lowest energy structure of O2 molecules on the C59N oxide. (c) The structure of C59NO2. (d)–(f) The optimized reaction paths for CO oxidization on C59N and its oxides catalysts. The initial, final, saddle, and meta-stable intermediate states are illustrated in the inset images. C, N, and O are represented by the grey, blue, and red balls. | |
3.1.4 Discussion on the catalytic properties of C60−nXn (X = B or N, and n = 1, 2). As discussed above, both C59B and C59N can catalyze CO oxidizations. The CO oxidization or the O2 dissociation occurs in the initial catalytic reaction on C59B and helps to produce a stable C59BO3 oxide catalyst, which could be further used repeatedly as a catalyst species. The CO oxidization on C59BO3 oxide is found to have a rate determining energy barrier of 0.59 eV, showing a good catalytic performance. By using C59N in the CO-rich conditions to provide sufficient CO to protect C59N against oxidization, it could be kept as a repeating catalyst species. The corresponding rate determining barrier is 0.44 eV, which also shows the good catalytic ability of N doped fullerene. If there is not enough CO gas to surround the C59N, it may also be oxidized during the reaction to form C59NO oxide. Compared to the C59N, the catalytic ability of C59NO is reduced, and would require 0.80 eV as a rate determining activation energy to oxidize CO in the successive oxidization cycles. Also, in order to facilitate further theoretical and experimental studies, we calculated the vibration properties of the initial and final states of the above described reaction paths and no imaginary frequency was found. An imaginary vibrational mode is found for the corresponding transition state. The calculated frequencies are provided in Fig. S3 in the ESI.†In addition to the singly doped fullerene, a low doping concentration structure will probably also be generated during the fabrication of doped fullerene. Previous studies have shown that the B(N) dopants prefer to separately substitute the carbon atom in fullerene.28–30 For example, the best doping configurations for the two B and N atoms are that the dopants substitutionally occupy the opposite sites of a C6 hexagon. In our studies, we have studied the catalytic properties of the best doping configurations of C58B2 and C58N2. Like the singly doped fullerene, they evolve into the oxide materials after the first few catalytic cycles for catalyzing CO oxidizations. When compared to the oxides of C59B and C59N, our calculations do not show obvious synergetic effects on the catalytic properties of the C58B2 and C58N2 oxides (see Fig. S1 and S2 in the ESI†).
3.2 BN-pair doped fullerene
In the experiment, the B and N can also co-doped in fullerene, and the B–N bond is probably formed in the lowest energy doping configuration. The B–N bonding obviously affects their effects upon the co-doped nanostructures, which could be used to engineer the physical and chemical properties of the carbon nanostructures. With the purpose of helping design high-performance nanostructures in the experiments, we also carried out careful studies on the BN-pair doped fullerene to shed light on the catalytic properties of the low-concentration substitution doping configurations of the B–N co-doped carbon nanostructures. The stability of the BN-pair doped fullerene has also been confirmed using FPMD simulations performed for 5 ps at 1000 K.
3.2.1 Catalytic properties of C58BN. The lowest energy doping configuration occurs when the BN pair substitutionally replaces a C–C pair. On C58BN, both the O2 and CO allow chemical adsorption. Fig. 4a and b shows the O2 adsorptions in the configurations with an O–O bond as being parallel to the fullerene, which have close adsorption energies (about −0.29 eV). In addition, we have also optimized the geometrical structure by placing O–O parallel above the B–N bond. During the optimization, the O2 would however be pushed away, which is reasonable considering the inert nature of the B–N bond. However, the doping destroys the ideal π-electron conjugate integrity on pure fullerene. By considering the substitutional arrangement of dopant atoms in C60 as the doping structural fragment (DSF) of the C58BN configuration, the other part which only consists of a C atom can be discussed as the undoped structural fragment (USF). The density of the π-electron distribution above the DSF would be reduced in comparison to the distribution above the USF, making the adjacent space between them active for gas molecule adsorption. Like the adsorption of CO onto the B doped fullerene, CO prefers the end-on adsorption configuration (see Fig. 4c), developing a C–B bond and releasing 0.34 eV of energy. In Fig. 4d, the co-adsorption of CO and O2 is illustrated. The shortest atomic distance between CO and O2 is 3.7 Å, hinting at the weak interaction between them. Our NEB method studies show a 1.22 eV energy barrier for the oxidization reaction to occur between them, which would reduce the possibility of this reaction occurring. Our results show that the B–N co-doped C60 has similar catalytic properties to the B–N co-doped graphene. In both cases, B serves as the active center.50
|
| Fig. 4 The structures of O2 adsorption (a) and (b), CO adsorption (c), and CO and O2 co-adsorption (d) on C58BN. (e) The structure of C58BNO2 oxide. (f) and (g) The reaction pathways for CO oxidization catalyzed by C58BNO2 oxide. C, B, N, and O are represented by the grey, pink, blue, and red balls. | |
3.2.2 Catalytic properties of the C58BN oxide. As with the B and N doped fullerene, the BN-pair doped fullerene can also be oxidized to form C58BNO2. This can be obtained by the dissociation of the pre-adsorbed O2 to produce atomic O atoms to oxidize the C58BN, for which the energy barrier is only around 0.12 eV. Also, providing the catalyst is to be used in CO-rich surrounding conditions, the first few CO oxidization cycles would also help generate the C58BNO2 oxide. As illustrated in Fig. 4e, our first-principles structural optimizations confirm that the configuration shown in the Fig. 4e is the lowest energy oxidization structure, in which the O oxidation occurs around the B atom. It is 2.19 eV lower in energy than the configuration in which the O oxidization occurred around the N atom. In addition, the oxidization around the B atom in the lowest energy configuration shown in Fig. 4e would in turn hinder the O2 adsorption around the N atom. Therefore, we propose that the Fig. 4e configuration accounts for the main oxide species and would dominate the catalytic performance accordingly. The O2 can be adsorbed onto the C58BNO2 oxide without an energy barrier, which has an absorption energy of −0.56 eV. Approximately a 0.65e charge transfer is found to occur between the C58BNO2 oxide and the adsorbed O2 molecule, which excites it into the 1Δg singlet state and elongates the O–O bond by 0.09 Å. In Fig. 4f and g, we have evaluated the catalytic properties. Surprisingly, the rate determining barrier is found to be only 0.42 eV along the entire catalytic cycle. In addition, our FPMD simulations also suggest the stability of C58BNO2 at 1000 K. As for the product of a single O atom adsorbed onto the C58BNO2 oxide (see the inset image in Fig. 4g), our structural optimization shows that the single atomic O would not move to the adjacent bridge site upon formation of a B–N bond. The inert BN bond helps keep it at on the top site to retain good reactivity to oxidize the CO molecule. Compared to the barriers of CO oxidation catalyzed by B or N doped fullerene, the BN-pair doping shows synergetic effects to enhance the catalytic properties correspondingly. Also, our calculations of the frequencies of the reactants and products only show positive frequencies, suggesting their stability in the experimental fabrications. Again, the calculation only shows one negative frequency for the corresponding transition state, confirming the validity of the elastic band method for searching for the saddle point (see Fig. S3, ESI†).
3.3 B3N and BN3 doped fullerene
In addition to the smallest stoichiometric BN-pair doping, we also estimated the nonstoichiometric B–N doping in fullerene. The B3N(BN3), with the N(B) being surrounded by three B(N) atoms, were used as examples to illustrate the B- and N-rich nonstoichiometric co-doping. The doping configurations are shown in Fig. 5a and b, which are confirmed by our structural optimizations as being the lowest energy doping configurations. We also performed 5 ps FPMD simulations at 1000 K for the lowest energy doping configurations of C56B3N and C56BN3, which suggested that they were stable.
|
| Fig. 5 (a)–(e) Structures of B3N and BN3 doped fullerenes and the corresponding gas molecule adsorption configurations on them. (f) and (g) The reaction pathways of CO oxidizations catalyzed by the C56B3N oxide. (h) and (i) Reactions catalyzed by C56BN3. C, B, N, and O are represented by the grey, pink, blue, and red balls. | |
3.3.1 Catalytic properties of C56B3N. In the C56B3N nanostructure, owing to the fact that the B atoms are separately distributed around the center N atom, the co-adsorption of O2 and CO on different B atoms is also well separated, which could hinder a direct reaction between them. Therefore, in our studies, we concentrated on examining the catalytic properties of the B atom and its nearest N or C atoms. Both O2 and CO were found to prefer being adsorbed on the B atom with −1.55 and −0.65 eV adsorption energies, respectively. The corresponding adsorption configurations are provided in Fig. 5c and d. The adsorbed O2 gains an approximately 1.33e charge from C56B3N, which elongates the O–O bond by 0.27 Å to transfer it from the triplet ground state to the singlet excited state. Starting from the small molecule adsorption states, we calculated three reactions, the dissociation of O2 to directly oxidize C56B3N, the oxidization of the incoming COs by the pre-adsorbed O2 to finally generate the C56B3N oxide, and the oxidization of the pre-adsorbed CO by the incoming O2 to finally obtain the C56B3N oxide. Judging by the largest energy barrier of 0.48 eV found in these reactions, the final oxide C56B3NO2 could be obtained. We have estimated the stability of C56B3NO2 using FPMD simulations, which was found to be well preserved during the 5 ps simulations at 1000 K. Then, using C56B3NO2 oxide as a prototype, we optimized the minimum energy reaction paths for successive CO oxidizations which are shown in Fig. 5f and g. An O2 molecule could be adsorbed onto B56B3NO2 to be activated to help oxidize an incoming CO and finally release an CO2 molecule. Our Bader charge analysis shows approximately a 0.70e charge gain of O2, which helps elongate the O–O bond by 0.10 Å. The largest energy barrier for the reactions shown in Fig. 5f is 0.33 eV. After this, one more CO molecule can react with the produced O atom to release another CO2 and restore the geometrical structure of B56B3NO2, allowing it to be used as recycled catalyst species in successive catalytic reaction cycles. The corresponding rate determining energy barrier is only 0.42 eV.
3.3.2 Catalytic properties of C56BN3. In the C56BN3 nanostructure, the B atom surrounded by three N atoms was also found to be an active site for gas molecule adsorption. Our calculations show that only O2 could be adsorbed, which can connect with the central B atom in the end-on adsorption state as shown in Fig. 5e. The adsorption energy is −1.41 eV and the O–O is elongated by 0.12 Å, activating the O2 into its 1Δg singlet state to help oxidize CO. Also, a charge gain of approximately 0.80e was found in our Bader analysis. During the process of CO approaching the O2, it encounters an energy barrier of 0.63 eV to react with the O2 to form an O–O–C–O complex species attached onto C56BN3 with an O–B and a C–C bond. Under the 0.3 eV activation energy, this meta-stale state could further release an CO2 molecule and leave an atomic O capped onto the central B. In contrast to the case of the single B doped fullerene, the surrounding B–N bonds help hinder the oxidization of C56BN3 to retain the atomic O atom, which can then be easily removed by catalyzing the successive CO oxidization. The energy barrier is 0.28 eV. Once the produced CO2 molecule is released, the C56BN3 can be restored, which can be used again in the successive CO oxidization cycles, showing good recycling properties.
3.3.3 Discussion on the catalytic properties of B3N and BN3 doped fullerenes. Based on the above described results, one can see that the active sites are located around the B atom in both the B3N and BN3 doped fullerenes, consisting of the BN-pair doped fullerene. The B3N doped fullerene can be oxidized after a few cycles for catalyzing CO oxidizations. The oxidized nanostructure is found to have good catalytic properties and good recycling properties. In contrast, the N atoms surrounding the central B in the BN3 doped fullerene can help maintain the geometric structure of C56BN3 for catalyzing the CO oxidization. The BN3 doped structure can be repeatedly used for catalyzing the CO oxidization with a rate determining energy barrier of 0.63 eV. In addition, we have studied the vibrational properties of the initial and final states of the CO oxidizations catalyzed by the B3N or BN3 doped fullerenes, which supports their stabilities (no negative frequencies). The corresponding transition state was found to have only one imaginary frequency, suggesting that it is the saddle point state (see Fig. S3, ESI†). Again, we used DSF to account for the doping structural fragment of the geometrical distribution of dopant atoms. Our studies show that the B dopant at either the edge of the DSF fragment or the site close to the edge may have good catalytic properties, and it would be worthwhile performing detailed experimental and theoretical studies in order to design high-performance and durable nanocatalysts.
4. Conclusions
Using elastic band method calculations based on first-principles studies, we have carefully studied low-concentration B and N doped and their co-doped fullerenes. Both C59B and C59N show good catalytic properties for catalyzing CO oxidization, which could also be capable of being oxidized during the first few catalytic reaction cycles. The corresponding oxides were found to have superior catalytic properties, which could be repeatedly used as a catalyst showing durable properties as well. The CO and O2 could be co-adsorbed onto C59B. The co-adsorption configurations require 0.48 or 0.44 eV activation energies to make the CO oxidization occur and produce a C59BO oxide simultaneously, which could be further oxidized in the successive CO oxidization processes to obtain a C59BO3 oxide. In addition, the single O2 adsorption on C59B can also oxidize it with a 0.24 eV barrier. Providing it is used in CO-rich conditions, C59N could retain its structure as a recycling catalyst for CO oxidization. A 0.44 eV rate determining barrier is found. Otherwise, after oxidizing the CO, the produced atomic O atom can overcome the 0.20 eV to oxidize the C59N. Both the C59B and C59N oxides could be used as durable recycling catalysts, which are found to have 0.59 and 0.80 eV rate determining energy barriers, respectively. Interestingly, the co-doping of B and N in low concentration doping fullerene may have superior catalytic properties. The BN-pair doped fullerene would also be oxidized. The produced C58BN oxide can help to oxidize CO with a 0.42 eV rate determining barrier. For the nonstoichiometric B3N and BN3 species, their doping in fullerene is also found to have superior catalytic properties. The B atoms either at the doping domain edge in B3N or at the doping center in BN3 are active sites. C56B3N can be oxidized during catalyzing CO oxidizations. The resulting C56B3N oxide has a rate determining barrier of 0.42 eV for catalyzing successive CO oxidizations. In C56BN3, the central B is protected by its surrounding N atoms against oxidization to remain as a recycling catalytic active site for CO oxidization, which is found to have a 0.63 eV rate determining energy barrier.
Conflicts of interest
There are no conflicts of interest to declare.
Acknowledgements
The authors gratefully acknowledge financial support from the National Natural Science Foundation of China (NSFC) (Grant No. 11674129).
References
- H. Falsig, B. Hvolbœk, I. S. Kristensen, T. Jiang, T. Bligaard, C. H. Christensen and J. K. Nørskov, Angew. Chem., Int. Ed., 2008, 47, 4835 CrossRef CAS PubMed.
- Z.-P. Liu and P. Hu, J. Am. Chem. Soc., 2002, 124, 14770 CrossRef CAS PubMed.
- H.-T. Chen, J.-G. Chang, S.-P. Ju and H.-L. Chen, J. Comput. Chem., 2010, 31, 258 CAS.
- J. L. C. Fajín, M. N. D. S. Cordeiro and J. R. B. Gomes, J. Phys. Chem. C, 2008, 112, 17291 CrossRef.
- J. Xu, T. White, P. Li, C. He, J. Yu, W. Yuan and Y.-F. Han, J. Am. Chem. Soc., 2010, 132, 10398 CrossRef CAS PubMed.
- H.-L. Chen, C.-H. Su and H.-T. Chen, Chem. Phys. Lett., 2012, 536, 100 CrossRef CAS.
- J. Zhang, H. Jin, M. B. Sullivan, F. C. H. Lim and P. Wu, Phys. Chem. Chem. Phys., 2009, 11, 1441 RSC.
- H.-Y. Su, M.-M. Yang, X.-H. Bao and W.-X. Li, J. Phys. Chem. C, 2008, 112, 17303 CrossRef CAS.
- X.-Q. Gong, Z.-P. Liu, R. Raval and P. Hu, J. Am. Chem. Soc., 2004, 126, 8 CrossRef CAS.
- J. T. Hirvi, T.-J. J. Kinnunen, M. Suvanto, T. A. Pakkanen and J. K. Nørskov, J. Chem. Phys., 2010, 133, 084704 CrossRef.
- S.-H. Oh and G. B. Hoflund, J. Catal., 2007, 245, 35 CrossRef CAS.
- H.-T. Chen, J. Phys. Chem. C, 2012, 116, 6239 CrossRef CAS.
- H.-T. Chen and J.-G. Chang, J. Phys. Chem. C, 2011, 115, 14745 CrossRef CAS.
- L.-C. Hsu, M.-K. Tsai, Y.-H. Lu and H.-T. Chen, J. Phys. Chem. C, 2012, 117, 433 CrossRef.
- M. Huang and S. Fabris, J. Phys. Chem. C, 2008, 112, 8643 CrossRef CAS.
- Z.-P. Liu, X.-Q. Gong, J. Kohanoff, C. Sanchez and P. Hu, Phys. Rev. Lett., 2003, 91, 266102 CrossRef.
- C.-M. Wang, K.-N. Fan and Z.-P. Liu, J. Am. Chem. Soc., 2007, 129, 2642 CrossRef CAS.
- G. Chen, S. J. Li, Y. Su, V. Wang, H. Mizuseki and Y. Kawazoe, J. Phys. Chem. C, 2011, 115, 20168 CrossRef CAS.
- X. Fan, J. Li and G. Chen, RSC Adv., 2017, 7, 17417 RSC.
- D. W. Yuan, Z. R. Liu and J. H. Chen, J. Chem. Phys., 2011, 134, 054704 CrossRef CAS.
- D. W. Yuan and Z. Zeng, J. Chem. Phys., 2004, 120, 6574 CrossRef CAS.
- J. Zhang, Z. Fu, Z. Yang and S. F. Li, Phys. Lett. A, 2012, 376, 3235 CrossRef CAS.
- Y.-P. Xie and X.-G. Gong, J. Chem. Phys., 2010, 132, 244302 CrossRef.
- X. Chen, Phys. Chem. Chem. Phys., 2015, 17, 29340 RSC.
- J. Duan, S. Chen, M. Jaroniec and S. Z. Qiao, ACS Catal., 2015, 5, 5207 CrossRef CAS.
- X. Fan, G. Zhang and F. Zhang, Chem. Soc. Rev., 2015, 44, 3023 RSC.
- Y. Zheng, Y. Jiao, M. Jaroniec and S. Z. Qiao, Angew. Chem., Int. Ed., 2013, 52, 3110 CrossRef CAS.
- M. R. Manaa, Solid State Commun., 2004, 129, 379 CrossRef CAS.
- M. R. Manaa, D. W. Sprehn and H. A. Ichord, J. Am. Chem. Soc., 2002, 124, 13990 CrossRef CAS.
- M. R. Manaa, H. A. Ichord and D. W. Sprehn, Chem. Phys. Lett., 2003, 378, 449 CrossRef.
- X. B. Hu, Y. T. Wu and Z. B. Zhang, J. Mater. Chem., 2012, 22, 15198 RSC.
- I. H. Lin, Y. H. Lu and H.-T. Chen, Phys. Chem. Chem. Phys., 2016, 18, 12093 RSC.
- I.-H. Lin, Y.-H. Lu and H.-T. Chen, J. Comput. Chem., 2017, 38, 2041 CrossRef CAS.
- R. Krishnan, S.-Y. Wu and H.-T. Chen, Carbon, 2018, 132, 257 CrossRef CAS.
- M. D. Esrafili, R. Mohammad-Valipour, S. M. Mousavi-Khoshdel and P. Nematollahi, ChemPhysChem, 2015, 16, 3719 CrossRef CAS PubMed.
- Y. Tang, W. Chen, Z. Shen, S. Chang, M. Zhao and X. Dai, Carbon, 2017, 111, 448 CrossRef CAS.
- Y. Tang, Z. Liu, X. Dai, Z. Yang, W. Chen, D. Ma and Z. Lu, Appl. Surf. Sci., 2014, 308, 402 CrossRef CAS.
- S. Sinthika, E. M. Kumar and R. Thapa, J. Mater. Chem. A, 2014, 2, 12812 RSC.
- S. Nigam and M. Chiranjib, ACS Nano, 2008, 2, 1422 CrossRef CAS.
- G. Kress and J. Furthmüller, Phys. Rev. B: Condens. Matter Mater. Phys., 1996, 54, 11169 CrossRef.
- G. Kress and D. Joubert, Phys. Rev. B: Condens. Matter Mater. Phys., 1999, 59, 1758 CrossRef.
- J. P. Perdew, K. Burke and M. Ernzerhof, Phys. Rev. Lett., 1996, 77, 3865 CrossRef CAS.
- G. Mills, H. Jónsson and G. K. Schenter, Surf. Sci., 1995, 324, 305 CrossRef CAS.
- G. Henkelman and H. Jónsson, J. Chem. Phys., 2000, 113, 9978 CrossRef CAS.
- G. Henkelman and H. Jónsson, J. Chem. Phys., 1999, 111, 7010 CrossRef CAS.
- W. Tang, E. Sanville and G. Henkelman, J. Phys.: Condens. Matter, 2009, 21, 084204 CrossRef CAS.
- Q. Z. Li, J. J. Zheng, J. S. Dang and X. Zhao, ChemPhysChem, 2015, 16, 390 CrossRef CAS.
- Y. Wang, M. Jiao, W. Song and Z. Wu, Carbon, 2017, 114, 393 CrossRef CAS.
- F. Gao, G. Zhao, S. Yang and J. Spivey, J. Am. Chem. Soc., 2013, 135, 3315 CrossRef CAS.
- C. Ricca, F. Labat, C. Zavala, N. Russo, C. Adamo, G. Merino and E. Sicilia, J. Comput. Chem., 2018, 39, 637 CrossRef CAS.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c9ra02172h |
|
This journal is © The Royal Society of Chemistry 2019 |
Click here to see how this site uses Cookies. View our privacy policy here.