 Open Access Article
 Open Access Article
Yafei Luoa, 
Zhongzhu Chena, 
Jin Zhang*b, 
Ying Tangb, 
Zhigang Xua and 
Dianyong Tang *ab
*ab
aInternational Academy of Targeted Therapeutics and Innovation, Chongqing University of Arts and Sciences, Chongqing 402160, P. R. China
bChongqing Key Laboratory of Environmental Materials and Remediation Technologies, Research Institute for New Materials Technology, Chongqing University of Arts and Sciences, Chongqing 402160, P. R. China. E-mail: Zhangjin@cqwu.edu.cn; tangdy2008@163.com
First published on 1st March 2017
Understanding the role of CeO2(111) supports is meaningful for designing high-performance metal oxide-supported gold nanoparticle catalysts. Here, density functional theory calculations were employed to study ω-alkynylfuran cycloisomerisation on CeO2(111)-supported Au clusters. The various reactive sites, including the atop, interface and edge sites, and the role of oxygen vacancies on the defective CeO2(111) surface were taken into account. On the basis of the computed results and energetic analysis, it was found that the atop and interface sites show high catalytic activity toward ω-alkynylfuran cycloisomerisation, and the edge site of Au10/CeO2(111)-s (stoichiometric) exhibits similar catalytic activity. Meanwhile, the surface oxygen vacancies of CeO2(111) can cause some negative and positive effects on the adsorption energy and the catalytic activity. Furthermore, to shed light on the role of the CeO2(111) support, an analysis of ω-alkynylfuran cycloisomerisation catalyzed by Au3–4/CeO2(111) and free Au3–4 clusters was performed as well. Our results indicate that the presence of the CeO2(111) support can not only change the orbital levels of the gold clusters, but also cause charge recombination and decrease the positive charge on the Au (top) atom. These virtues can effectively lead to a decrease in the adsorption energy, facilitating electrophilic attack of the C atom on the furan ring.
CeO2-supported Au catalysts have been regarded as promising catalytic systems because they include two highly active components, namely, the CeO2 surface and Au nanoparticles.12,13 Ciftci et al. prepared a set of catalysts with Au and Pt supported on CeO2 nanorods and nanocubes, which were applied as catalysts in the decomposition of ethanol and formic acid.14 They found that Au catalysts are more active and selective toward H2 than Pt catalysts in formic acid decomposition. Fu and coworkers reported that nanostructured gold–cerium oxide catalysts are active for the water–gas shift reaction.15 Based on the studied results, they found that the metal nanoparticles do not take part in the reaction, and that the reaction is actually catalyzed by non-metallic gold species strongly associated with surface cerium oxygen groups. Han and colleagues prepared low Au-loaded CeO2 nanoparticle catalysts with high activity via several solution chemistries, and used them as catalysts for low-temperature CO oxidation.16 They discovered that the Au-loaded CeO2 nanoparticle catalysts exhibit high catalytic activity because of their large surface area as well as the coexistence of Auδ+ (Au+ and Au3+) and Au0 species, in which Au+ plays a predominant role. Therefore, in order to recognize and design a highly active ceria-based catalyst, it is extremely important to illustrate the nature of the active sites and the catalytic activity of CeO2-supported Au nanoparticles in detail.
Lattice oxygen atoms17 and under-coordinated Au atoms in Au nanoparticles18 have both been reported as reactive species for CO oxidation catalyzed by CeO2-supported Au nanoparticles. CO oxidation, as a prototypical reaction in heterogeneous catalysis,19 has attracted enormous attention and has been extensively studied. Kim et al. compared CO oxidation by Au13 nanoparticles supported on stoichiometric and partially reduced CeO2 with the help of DFT+U calculations, and confirmed the critical role of oxygen vacancies in the CeO2 surface. They also suggested that lowering the vacancy formation energy of the CeO2 surface is a promising method for enhancing the CO catalytic activity.11 Additionally, analysis shows that CO oxidation by the Mars–van Krevelen mechanism at the interface between doped CeO2 and supported Au nanoparticles is more effective than that at undoped CeO2 surfaces.20 In general, for nanocatalysts, it is meaningful to understand the interface effects of metal/support catalysts. The interface between the metal nanoparticles and the oxide supporting materials can cause a pronounced effect on the catalytic activity.21–23 Recently, on the basis of a theoretical study, Bing Liu et al. explored the three reaction mechanisms for CO oxidation on CeO2-supported Pd nanorods, that is, the Pd-Ce3+ dual site mechanism, M–vK mechanism and Pd-only mechanism.24 By analyzing the calculated results, they found that interface effects play a crucial role and can strongly affect the catalytic activity, which can be understood by considering the structural and electronic properties of the materials. In subsequent work, CO oxidation on CeO2-supported Pd bimetallic nanorods was investigated by means of a theoretical method and it was found that CO and O2 can bind at different sites on Pd-Ag/CeO2 and Pd-Cu/CeO2.25 The results suggested that both the Pd-Ag and Pd-CeO2 interfaces in Pd-Ag/CeO2 can play a vital effect on CO oxidation. However, according to some previous reports,4,26 the catalytic activity of oxide-supported Au nanoparticles originates predominantly from the Au nanoparticles themselves, and the oxide surface is regarded as a stabilizer for the Au nanoparticles. Therefore, without doubt, knowledge of the reactive species, including the oxygen vacancies and under-coordinated Au atoms, and the interface between the Au nanoparticles and the supporting material, is meaningful for designing high-performance catalysts and understanding the origin and nature of the catalytic activity.27–30
In order to achieve this goal, the mechanism of ω-alkynylfuran cycloisomerisation on CeO2(111)-supported subnanometer gold clusters is investigated via a theoretical study in this article. Cycloisomerisation is an effective strategy used to obtain phenols and their derivatives, which is extensively used to synthesize natural products, polymers and pharmaceuticals.31–36 According to a previous study, Au/CeO2 can efficiently catalyze cycloisomerisation, leading to a high conversion ratio.35 However, to date, the mechanism of ω-alkynylfuran cycloisomerisation catalyzed by CeO2-supported gold nanoparticles has not been elaborated or unveiled in detail. Herein, ω-alkynylfuran cycloisomerisation catalyzed by CeO2-supported gold nanoparticles (Au3, Au4, Au10, Au11) is explored with the help of density functional theory (DFT), as an expansion of our prior research.37–39 Gold nanoparticles (Au3, Au4, Au10, Au11) were employed for consistence with experimental results reported by Oliver-Meseguer et al. and others.40–42 In these studies, it was found that small gold clusters (only 3 to 10 atoms in size) can be formed during the catalytic processes, which can catalyze the ω-alkynylfuran cycloisomerisation reaction. In this paper, only the 5-exo Friedel–Crafts-type reaction pathway was investigated, and other possible reaction pathways were not considered. The 5-exo Friedel–Crafts-type mechanism (FCT) is the most feasible pathway of ω-alkynylfuran cycloisomerisation to produce the targeted phenol derivative product, catalyzed by subnanometer gold clusters and planar gold clusters, based on our previous reports.37–39 In order to illustrate the catalytic role of the supporting material, stoichiometric CeO2 and partially reduced CeO2 with one vacancy are also considered here. In addition, the possible catalytic sites of Aun/CeO2(111), including the atop, edge and interface sites, are investigated, aiming to illustrate the catalytic activity of the catalytic sites and interfacial effects. Other clusters, such as Pd, Pt or Ag clusters, supported on the surface of CeO2 will be employed in future work to explore the effect of different clusters on the catalytic properties for ω-alkynylfuran cycloisomerisation.
It is well-known that the CeO2(111) surface is the most thermodynamically stable among the three low-index surfaces of ceria, that is, CeO2(111), CeO2(110) and CeO2(100), implying that the CeO2(111) surface is the most commonly exposed surface of ceria.8,52 Therefore, a 4 × 4 CeO2(111) slab with 6 atomic layers53,54 was employed to describe the stoichiometric CeO2 surface (CeO2-s) and the reduced surface (with gold clusters on an oxygen vacancy, CeO2-v), and 30 Å of vacuum (Fig. 1) was used in order to minimize the interaction between cells. During the geometry optimization, the three upper atomic layers of the CeO2 slab were relaxed, while the other remaining atomic layers were fixed. Consideration of the enough large surface cells for all models, only a gamma-point mesh was chosen for Brillouin zone integration. In addition, the bulk equilibrium lattice constant (5.44 Å) was calculated by means of the PBE/DNP method with 8 × 8 × 8 k-points, which is consistent with the experimental values55 and previous theoretical studies.56–58
|  | ||
| Fig. 1 A 4 × 4 CeO2(111) slab is used to model (a) stoichiometric CeO2 and (b) partially reduced CeO2 with one vacancy. | ||
Usually, to correct the resulting electronic structure of reduced ceria, the Hubbard-U term in the DFT+U approach is employed. However, according to a paper reported by Da Silva et al., a reasonable description of the structural parameters, relative energies of different oxides and spectroscopic properties cannot be given at the same time using a unique value of U; therefore, it is not clear whether the DFT+U method provides a systematic improvement of the energetics.59 In addition, in Bernard Delley and coworkers' reports, the stability and morphology of cerium oxide surfaces in an oxidizing environment, the adsorption and thermodynamic stability of CHx (x = 1–4) on a CeO2(111) surface, and water adsorption on stoichiometric and reduced CeO2(111) surfaces were explored by employing the DFT-GGA approach using Dmol3 software and the results were reliable and comparable.60–62 The same choice was made to study CO adsorption on CeO2 and investigate the interaction of water with stoichiometric and reduced CeO2 surfaces by Yang et al. and Kumar et al., respectively.63,64 Hence, in view of these considerations, the DFT-GGA approach is also adopted in this article.
Additionally, herein, the turnover frequency (TOF) was employed to evaluate the efficiency of a catalytic cycle. The energetic span model can be used to predict the TOF from theoretically obtained free energy profiles, which was proposed by Shaik and co-workers.65–68 The Gibbs free energy is related to the corrected enthalpy (ΔHcorrect) and entropy (ΔS). These two parameters were not considered because numerical frequency computations are difficult for large system in Dmol3. On the basis of this model, the TOF-determined transition state (TDTS) and intermediate (TDI) can be determined by evaluating the degree of TOF control (XTOF,i), as shown in eqn (1):
|  | (1) | 
|  | (2) | 
|  | (3) | 
All of the kinetic information was obtained by applying the energetic span model using the AUTOF program.67
|  | ||
| Fig. 2 The most stable structures of gold clusters on CeO2(111) and possible catalytic sites of Aun/CeO2(111). | ||
|  | ||
| Fig. 3 Charge density difference of Aun/CeO2(111) (blue and yellow isosurfaces represent increasing and decreasing electron densities, respectively; isovalue = 0.03). | ||
![[double bond, length as m-dash]](https://www.rsc.org/images/entities/char_e001.gif) C2 bond or C1 site of the furan ring (abbreviated as 5-exo FCT). The second pathway is [4 + 2] cycloaddition between the C
C2 bond or C1 site of the furan ring (abbreviated as 5-exo FCT). The second pathway is [4 + 2] cycloaddition between the C![[triple bond, length as m-dash]](https://www.rsc.org/images/entities/char_e002.gif) C bond and the C1
C bond and the C1![[double bond, length as m-dash]](https://www.rsc.org/images/entities/char_e001.gif) C2–C3
C2–C3![[double bond, length as m-dash]](https://www.rsc.org/images/entities/char_e001.gif) C4 of the furan ring to produce the final product (abbreviated as DDA). The last pathway is direct hydrogen transfer from the Cα atom to the Cβ atom to form an Au-vinylidene carbenoid intermediate, and subsequent Diels–Alder addition of the Cα–Cβ double bond to the furan ring (abbreviated as VDA). Additionally, there is a 6-endo FCT pathway, which involves the nucleophilic addition of a Cα atom to the furan ring in IM1 in competition with the 5-exo FCT pathway, finally leading to a pyran derivative. Moreover, the Cβ atom can attack the C2 atom of the furan ring, finally obtaining a β-alkenylated furan via H migration. The energy profiles for all of the possible mechanisms are depicted in Fig. 4–7. For the VDA route, H migration requires a large energy barrier to be overcome, and therefore it is not taken into account. According to Fig. 4–7, the rate-limiting step of the 5-exo FCT reaction route in the gas phase is the nucleophilic addition of the Cβ atom to the C1 site of the furan ring to form the spiro-intermediate IM2, which has an energy barrier of 13.66 kcal mol−1, while the formation of IM4 is the rate-determining step in acetonitrile. However, for the DDA pathway, the formation of the β-alkenylated furan and the 6-endo FCT pathway, the energy barriers of the rate-limiting steps are 46.28 (44.80), 28.79 (27.86) and 35.26 (35.87), respectively. Obviously, the 5-exo FCT reaction route is the most feasible pathway for ω-alkynylfuran cycloisomerisation to produce the targeted phenol derivative product.
C4 of the furan ring to produce the final product (abbreviated as DDA). The last pathway is direct hydrogen transfer from the Cα atom to the Cβ atom to form an Au-vinylidene carbenoid intermediate, and subsequent Diels–Alder addition of the Cα–Cβ double bond to the furan ring (abbreviated as VDA). Additionally, there is a 6-endo FCT pathway, which involves the nucleophilic addition of a Cα atom to the furan ring in IM1 in competition with the 5-exo FCT pathway, finally leading to a pyran derivative. Moreover, the Cβ atom can attack the C2 atom of the furan ring, finally obtaining a β-alkenylated furan via H migration. The energy profiles for all of the possible mechanisms are depicted in Fig. 4–7. For the VDA route, H migration requires a large energy barrier to be overcome, and therefore it is not taken into account. According to Fig. 4–7, the rate-limiting step of the 5-exo FCT reaction route in the gas phase is the nucleophilic addition of the Cβ atom to the C1 site of the furan ring to form the spiro-intermediate IM2, which has an energy barrier of 13.66 kcal mol−1, while the formation of IM4 is the rate-determining step in acetonitrile. However, for the DDA pathway, the formation of the β-alkenylated furan and the 6-endo FCT pathway, the energy barriers of the rate-limiting steps are 46.28 (44.80), 28.79 (27.86) and 35.26 (35.87), respectively. Obviously, the 5-exo FCT reaction route is the most feasible pathway for ω-alkynylfuran cycloisomerisation to produce the targeted phenol derivative product.
|  | ||
| Fig. 4 Energy profile of the 5-exo FCT pathway that was used to form the phenol derivative P1 in the gas phase and acetonitrile solvent (parentheses). | ||
|  | ||
| Fig. 5 Energy profile of the DDA pathway that was used to form the phenol derivative P1 in the gas phase and acetonitrile solvent (parentheses). | ||
|  | ||
| Fig. 6 Energy profile for the formation of the β-alkenylated furan P2 in the gas phase and acetonitrile solvent (parentheses). | ||
|  | ||
| Fig. 7 Energy profile of the 6-endo Friedel–Crafts-type (FCT) pathway that was used to form the pyran derivative P3 in the gas phase and acetonitrile solvent (parentheses). | ||
|  | ||
| Fig. 8 The optimized structures of ω-alkynylfuran cycloisomerisation catalyzed by the atop site of Au10/CeO2(111)-s. | ||
Firstly, ω-alkynylfuran cycloisomerisation on the atop sites of Au10/CeO2(111) and Au11/CeO2(111) is discussed. As shown in Fig. 5–8, the adsorption of ω-alkynylfuran on the atop sites is exothermic by about 15–18 kcal mol−1 in the gas phase and acetonitrile solvent (Ca (catalyst) + Sub (substrate) → IM1 (intermediate)). The adsorption energies of the substrates on the atop sites of the gold clusters supported on the CeO2(111) surfaces are comparable with those on subnanometer gold clusters (Au38, Au27, Au28, Au30, Au35 and Au55).38 In addition, analysis of the computed adsorption energies exhibited in Fig. 5–8 suggests that the surface O vacancy of CeO2(111) only has a slight influence on the adsorption of the substrate on the atop sites. Once the ω-alkynylfuran is adsorbed on the atop sites of the gold clusters supported on the CeO2(111) surfaces, the Cβ atom electrophilically attacks the furan ring to give rise to a spiro-intermediate, IM2 (IM1 → IM2). This step is kinetically feasible, with an energy barrier of about 5 kcal mol−1. In addition, the IM1 → IM2 conversion step is exothermic by about 5–8 kcal mol−1 in acetonitrile solvent. Subsequently, the cleavage of the C–O bond of the furan ring in IM2 produces a linear conjugate triene ketone intermediate (IM3) through transition state TS2/3 with an energy barrier of 8–9 kcal mol−1. This step is nearly thermoneutral in acetonitrile solvent. In the next step, an oxygen atom from a carbonyl group approaches the Au–C bond yielding an oxepine intermediate (IM4), which is exothermic in both the gas phase and acetonitrile solvent with an energy barrier of about 8–11 kcal mol−1. Finally, oxepine is desorbed from the oxepine intermediate to recover the catalyst. This step is endothermic by about 8–18 kcal mol−1. The oxepine then quickly converts into the phenol product with an exothermicity of about 40 kcal mol−1 upon heating or exposing to acid.33,34,70 Additionally, on the basis of the energetic span model by Shaik and coworkers, the TOF values of ω-alkynylfuran cycloisomerisation on the atop, interface-corner, interface-edge and edge sites are calculated and shown in the Table 1. Compared with ω-alkynylfuran cycloisomerisation on the interface-corner, interface-edge and edge sites, the atop site has larger TOF values of about 105 to 106 s−1, indicating that the atop site possesses high catalytic activity. Clearly, the catalytic activity of the atop sites is similar to that of subnanometer gold clusters, due to the similar binding characters of the gold atoms. Acetonitrile solvent can have a slight influence on the energy barriers and the reaction rates.
| TDI/TDTS | δE (kcal mol−1) | TOF (s−1) | |
|---|---|---|---|
| Au10/CeO2(111)-s | |||
| Atop | IM2/TS3/4 | 11.09 | 2.9 × 105 | 
| Interface-corner | IM2/TS3/4 | 14.03 | 4.1 × 103 | 
| Interface-edge | IM3/TS3/4 | 16.03 | 4.3 × 102 | 
| Edge | IM2/TS3/4 | 13.32 | 2.0 × 104 | 
| ![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) | |||
| Au10/CeO2(111)-v | |||
| Atop | IM3/TS3/4 | 10.98 | 3.3 × 105 | 
| Interface-corner | IM3/TS3/4 | 29.93 | 1.6 × 10−7 | 
| Interface-edge | IM3/TS3/4 | 13.93 | 4.9 × 103 | 
| Edge | IM3/TS3/4 | 29.93 | 1.6 × 10−7 | 
| ![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) | |||
| Au11/CeO2(111)-s | |||
| Atop | IM2/TS3/4 | 9.79 | 1.2 × 106 | 
| Interface | IM3/TS3/4 | 13.75 | 6.5 × 103 | 
| Edge | IM3/TS3/4 | 22.21 | 1.3 × 10−2 | 
| ![[thin space (1/6-em)]](https://www.rsc.org/images/entities/char_2009.gif) | |||
| Au11/CeO2(111)-v | |||
| Atop | IM4/IM5 | 14.46 | 1.1 × 103 | 
| Interface | IM3/TS3/4 | 10.44 | 6.6 × 105 | 
| Edge | IM3/TS3/4 | 25.89 | 7.1 × 10−5 | 
Subsequently, ω-alkynylfuran cycloisomerisation on the edge sites of Au10/CeO2(111) and Au11/CeO2(111) were investigated and discussed. The adsorption energies are smaller as compared to that of the atop sites because of the higher coordination numbers of the edge sites. Interestingly, a distinctive substrate adsorption behavior is observed for the edge site of Au11/CeO2(111)-v. As shown in Fig. S14,† the adsorption of the substrate on the edge site of Au11/CeO2(111)-v induces strong structural deformation of the Au11 fragment due to the strong interaction between the adsorbed alkyne group and the Au atoms. The corresponding structural deformation raises the energy barrier for the electrophilic attack of the C atom on the furan ring. The electrophilic attack of the C atom on the furan ring (IM1 → IM2) and the cleavage of C–O in the furan ring (IM2 → IM3) steps on the edge sites have similar energy barriers. The closure of the ring to form the oxepine intermediate on the edge site of Au10/CeO2(111)-s needs to overcome an energy barrier of 10.21 (12.12) kcal mol−1 in the gas phase (acetonitrile solvent), which is comparable to the situation on the atop site. However, the closure of the ring to form the oxepine intermediate on the edge site of Au10/CeO2(111)-v and Au11/CeO2(111)-v entails a large energy barrier of about 29 kcal mol−1 due to the μ2-coordination in IM3. Simultaneously, the closure of the ring to form the oxepine intermediate on the edge site of Au11/CeO2(111)-s must overcome an energy barrier of about 20.00 kcal mol−1 due to the large deformation of the substrate fragment. Hence, only the edge sites of Au10/CeO2(111)-s show similar catalytic activity toward ω-alkynylfuran cycloisomerisation to the atop sites.
Finally, the 5-exo FCT mechanism can be extended to the interface sites of Au10/CeO2(111) and Au11/CeO2(111), so ω-alkynylfuran cycloisomerisation on the interface sites of Au10/CeO2(111) and Au11/CeO2(111) is also explored. As seen from Fig. 9–12, there are two types of interface sites for Au10/CeO2(111)-s and Au10/CeO2(111)-v. In contrast, the interface sites of Au11/CeO2(111)-s and Au11/CeO2(111)-v have similar bonding character, and hence there is only one type of interface site. The adsorption of the substrate on the interface sites causes a large structural deformation of the supported gold clusters due to the strong interaction between the alkyne group and gold atoms. The large structural deformation of the supported gold clusters counteracts the partial stabilizing interaction between the alkyne group and the gold atoms, which results in lower adsorption energies of the substrate on the interface sites. For the interface sites, the closure of the ring to form the oxepine intermediate is the rate-limiting step in both the gas phase and acetonitrile solvent. The interface-corner sites of Au10/CeO2(111)-v may be viewed as inactive toward ω-alkynylfuran cycloisomerisation compared to the other interface sites, due to the formation of μ2-coordination in IM3. The catalytic activity of the interface sites of Au10/CeO2(111) is lower than that of the atop sites. Acetonitrile solvent enhances the energy barrier of the closure of the ring to form the oxepine intermediate and reduces the reaction rate.
In order to illustrate the adsorption properties of ω-alkynylfuran on the different sites of Au10/CeO2(111), the corresponding local density of states (LDOS) are calculated and shown in Fig. 13 and S15.† In this article, the LDOS discussion only focuses on the d-band information because the valence orbitals are the s and d orbitals of gold. Moreover, the interaction between the clusters and the ω-alkynylfuran depends on π-back-donation and σ-coordinate bonding, that is, charge transfer between the d and π* orbitals or π and d* orbitals. Hence, the d-band information is mainly investigated in this article.71 According to Fig. 13 and S15,† the bands of the adsorbed alkyne and Au10/CeO2(111) moved to the left toward the lower energy region, compared with the free substrate and Au10/CeO2(111). The main peak of the alkyne overlapped with those of the different sites of Au10/CeO2(111), indicating chemical bond formation between the substrate and Au10/CeO2(111). Compared with the interface-corner, interface-edge and edge sites, the band of the adsorbed alkyne is more down-shifted for the atop site and the main peaks of the alkyne are more effectively overlapped with the atop site, leading to a larger adsorption energy. In addition, the adsorption energies of ω-alkynylfuran on the interface-edge sites of Au10/CeO2(111) (stoichiometric and reduced) exhibit obvious differences, which can be attributed to the intensity and overlap degree of the bands.
Similarly, the local density of states (LDOS) are calculated again to elaborate the adsorption of ω-alkynylfuran on Au11/CeO2(111) (stoichiometric and reduced). Based on the computed results, the adsorption energy of ω-alkynylfuran on the interface sites is larger than that on the atop and edge site owing to the better overlap of the peaks, which can be seen from Fig. S16.† Compared with the edge sites, the band of the absorbed alkyne is more down-shifted and there is better overlap of the peaks for the alkyne and the atop Au atoms, leading to larger adsorption energies. However, for the adsorption of ω-alkynylfuran on Au11/CeO2(111) (vacancy, Fig. S17†), the adsorption energy is the smallest at the interface sites due to the weak d peak at around 8 eV and the relatively weak overlap of the bands.
In summary, according to the above-mentioned analyses, the atop and interface sites exhibit high catalytic activity toward ω-alkynylfuran cycloisomerisation via the FCT mechanism. The edge sites of Au10/CeO2(111)-s show similar catalytic activity toward ω-alkynylfuran cycloisomerisation to the atop sites. The adsorption energies of the substrate on the atop sites of the gold clusters supported by the CeO2(111) surfaces are comparable with those on subnanometer gold clusters. Due to the higher coordination number of the edge and interface sites, lower adsorption energies of the substrate on the edge and interface sites were identified. In addition, based on the calculated results, it is found that the surface O vacancy of CeO2(111) has some negative and positive influences on the adsorption energies of the substrate and the catalytic activity.
Additionally, the mechanisms of ω-alkynylfuran cycloisomerisation catalyzed by Au4/CeO2(111)-s, Au4/CeO2(111)-v and free Au4 clusters are also unveiled. As shown in Fig. 15, the catalytic cycles of ω-alkynylfuran cycloisomerisation on Au4/CeO2(111)-s, Au4/CeO2(111)-v and free Au4 clusters are similar to those on Au10/CeO2(111), Au11/CeO2(111), Au3/CeO2(111) and free Au3, including the adsorption of the ω-alkynylfuran, the formation of the Cβ–C1 bond, the breakage of the C1–O bond in the furan ring, and the formation of the seven-membered ring. On the basis of the energy profiles, the supported Au4 clusters are clearly more active than the free Au4 clusters toward ω-alkynylfuran cycloisomerisation.
According to the calculated results, the rate-determining steps of ω-alkynylfuran cycloisomerisation on CeO2-supported Au3/Au4 and free Au3/Au4 are the formation of the Cβ–C1 bond, that is, the IM1 → IM2 conversion. Compared with free Au3, the CeO2 supporting material can efficiently facilitate ω-alkynylfuran cycloisomerisation, decreasing the energy barriers for IM1 → IM2 conversion to 2.69–2.79 (2.04–2.78) kcal mol−1 in the gas phase (acetonitrile solvent). In addition, the oxygen vacancy can have a minor effect on the energy barriers for ω-alkynylfuran cycloisomerisation on Au3/CeO2 in the gas phase (acetonitrile solvent). Similarly, compared with free Au4, CeO2-supported Au4 can decrease the energy barriers of the rate-determining step to 8.96–13.28 (6.86–11.30) kcal mol−1 in the gas phase (acetonitrile solvent), indicating the active role of CeO2 in ω-alkynylfuran cycloisomerisation.
In order to better illustrate the catalytic reactivity of the free gold clusters and supported gold clusters, the corresponding energetic span (δE) and TOF values were calculated and the values are given in Table 2. As shown in Table 2, the TOF values for ω-alkynylfuran cycloisomerisation catalyzed by free Au3–4 are smaller than those for Au3–4/CeO2(111). Therefore, the presence of CeO2(111) can effectively facilitate ω-alkynylfuran cycloisomerisation.
| TDI/TDTS | δE (kcal mol−1) | TOF (s−1) | |
|---|---|---|---|
| Au3 | IM4/IM5 | 27.45 | 3.3 × 10−6 | 
| Au3/CeO2(111)-s | IM4/TS3/4 | 10.92 | 2.3 × 105 | 
| Au3/CeO2(111)-v | IM3/TS3/4 | 11.02 | 3.0 × 105 | 
| Au4 | IM2/IM5 | 16.94 | 13 × 101 | 
| Au4/CeO2(111)-s | IM3/IM5 | 11.26 | 7.4 × 104 | 
| Au4/CeO2(111)-v | IM3/TS3/4 | 9.27 | 2.2 × 106 | 
| Footnote | 
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c6ra27207j | 
| This journal is © The Royal Society of Chemistry 2017 |