Abstract
Supercages of faujasite (FAU)‐type zeolites serve as a robust scaffold for stabilizing dinuclear (Mo2S4) and tetranuclear (Mo4S4) molybdenum sulfide clusters. The FAU‐encaged Mo4S4 clusters have a distorted cubane structure similar to the FeMo‐cofactor in nitrogenase. Both clusters possess unpaired electrons on Mo atoms. Additionally, they show identical catalytic activity per sulfide cluster. Their catalytic activity is stable (>150 h) for ethene hydrogenation, while layered MoS2 structures deactivate significantly under the same reaction conditions.
Keywords: EPR spectroscopy, hydrogenation, molybdenum sulfide clusters, transition metal sulfides, zeolites
Dinuclear (Mo2S4) and tetranuclear (Mo4S4) molybdenum sulfide clusters were synthesized within the supercages of a faujasite zeolite. Encaged Mo4S4 clusters possess a structure similar to the nitrogenase enzyme's FeMo‐cofactor; both contain unpaired electrons and show identical catalytic activity per cluster. Their activity for ethene hydrogenation is stable, while layered MoS2 deactivates significantly under the same conditions.

Sulfide‐based enzymes and the success of transition metal sulfide (TMS) catalysts for hydrotreating reactions have spurred wide interests to understand their activity and selectivity and especially the impact of the cluster size and structure for reductive catalysis. For the nitrogenase family, three TMS clusters have been identified acting as catalytically active sites, i.e., a Fe4S4 tetramer, the P‐cluster (Fe8S7) and a third cluster Fe7MS9C (M=Fe, Mo, V); the Mo form, the so‐called FeMo‐cofactor, is the most intensively studied one among the Fe7MS9C family of clusters. [1]
The structures of the active site in the layered TMS materials have been equally well investigated compared to those in enzyme‐based catalysts. In addition to the use of the former as hydrogenation and hydro‐defunctionalization catalysts for hydrotreating of refinery fractions and renewable feedstocks, [2] TMS have recently drawn major interest as cathode materials in electrocatalysis. [3] Despite their similar chemical compositions, the TMS clusters in enzymes are well‐defined entities, whereas TMS phases in industrial catalysts for hydrotreating predominantly form significantly larger slab‐like structures. [4]
To achieve greater catalytic efficiencies, enzyme TMS clusters served as inspirations for the synthesis of active hydrogenation sites.[ 1e , 5 ] Most of the prior studies focused on multi‐step syntheses of TMS clusters and on using them as homogeneous organometallic catalysts in liquid phase. [6] A one‐step synthesis could, in contrast, enable the use of such entities as potentially robust highly efficient catalysts. In this context, zeolites represent a promising group of porous supports that provide a stable and well‐defined steric environment for the TMS clusters, mimicking partly the pockets of enzymes that host the active center.
Among the methods reported for immobilizing Mo and NiMo sulfide clusters on/in zeolites, ion exchange proves useful yet requires intricate synthesis of the cationic clusters. [7] Even worse, the groups of Tatsumi and Breysse reported that the zeolite‐confined TMS clusters decomposed into MoS2 slabs under reaction conditions.[ 7a , 7b ] This structural degradation is likely caused by the presence of water after ion exchange. [8]
Using leads from Okamoto et al., [9] we used chemical vapor deposition (CVD) and subsequent thermal treatments in reactive gases to incorporate homotopic size‐ and structure‐selective MoxSy clusters into the pores of zeolite NaY. The (uniformity of the) geometric structure and the spin state of the MoxSy clusters were acquired in the present study by combining X‐ray absorption spectroscopy (XAS), X‐ray emission spectroscopy (XES), electron paramagnetic resonance (EPR) spectroscopy, and density functional theory (DFT) calculations. A close similarity was revealed between the tetranuclear Mo4S4 cluster and the Mo site in nitrogenase enzymes. These NaY‐encaged MoxSy clusters displayed outstanding stability for ethene hydrogenation, much superior to that of a traditional slab‐MoS2 catalyst.
Mo(CO)6 encapsulated in a NaY zeolite was treated in H2S/H2 at 673 K for 2 h to form MoxSy species within the zeolite (MoxSy/NaY‐sulf). The zeolite used was almost free of extra‐framework Al (EFAl) and remained so after loading Mo and sulfidation (Figure S1). This catalyst was subsequently reduced in pure H2 (MoxSy/NaY‐red) at 673 K for 2 h. Figure 1 shows the k3‐weighted extended X‐ray absorption fine structure (EXAFS) and Fourier‐transformed (FT) EXAFS of these catalysts at Mo K‐edge. The corresponding fitted parameters are reported in Table 1. For MoxSy/NaY‐sulf, the Mo‐S and Mo‐Mo coordination numbers (CN) and interatomic distances (d) together with the S/Mo ratio of ≈2 (determined by elemental analysis) point to the overall cluster composition of Mo2S4. We hypothesize that in this structure, each Mo atom is coordinated to two bridging S atoms and one terminal S atom (either in cis or in trans configuration), resulting in theoretical CNMo‐Mo≈1 and CNMo‐S≈3. Slightly higher measured coordination numbers (CNMo‐Mo≈3.9; CNMo‐S≈1.3) are attributed to a minor presence of higher nuclearity species (e.g., a few MoS2 slabs on the external surface of the zeolite). For MoxSy/NaY‐red, the observed CNMo‐Mo and CNMo‐S together with the S/Mo ratio of ≈1 suggest the reduced state to be a Mo4S4 cluster. Additionally, based on similar values of dMo‐Mo and dMo‐S, we hypothesize the Mo4S4 cluster to resemble a distorted Mo4‐tetrahedron with an S atom sitting on each face. The composition and structure of this reduced state is different from a previously proposed Mo4S6 cluster with a cubane‐like structure. [9] Instead, we propose that the deduced structure has a close similarity with the MoFe3S3C subunit of the nitrogenase FeMo‐cofactor (Table 1). The MoxSy/NaY‐red catalyst was resulfided in H2S/H2 at 673 K for 2 h to form MoxSy/NaY‐resulf. The observed Mo‐Mo and Mo‐S CN and interatomic distances in MoxSy/NaY‐resulf were similar to those in MoxSy/NaY‐sulf, suggesting that the transformation between the sulfided and reduced structures is reversible by switching between pure H2 and H2S/H2 (Figure 3). [9]
Figure 1.

k3‐weighted EXAFS and FT EXAFS of MoxSy/NaY‐sulf (a,b), MoxSy/NaY‐red (c,d), and MoxSy/NaY‐resulf (e,f) catalysts. Experimental data is shown as closed symbols and the corresponding fits are shown as solid lines.
Table 1.
EXAFS fitting parameters: coordination numbers (CN), interatomic distances (d), E 0, ΔE 0, and Debye–Waller factors (σ2), for Mo–Mo and Mo–S paths in MoxSy/NaY‐sulf/red catalysts. CNMo‐Fe, CNMo‐S, dMo‐Fe and dMo‐S of the nitrogenase FeMo‐cofactor are added for comparison.
|
|
Path |
CN |
d [Å] |
E 0 [eV] |
ΔE 0 [eV] |
σ2×1000 [Å2] |
R‐factor |
|---|---|---|---|---|---|---|---|
|
MoxSy/NaY‐sulf |
Mo–S |
3.9±0.8 |
2.42±0.01 |
19 997 |
0.1±2.4 |
6.6±1.5 |
0.027 |
|
Mo–Mo |
1.3±1.1 |
2.77±0.03 |
10.3±8.6 |
||||
|
MoxSy/NaY‐red |
Mo–S |
2.6±1.4 |
2.47±0.05 |
19 995 |
0.4±5.0 |
5.5±5.0 |
0.039 |
|
Mo–Mo |
3.3±2.0 |
2.66±0.03 |
6.3±2.6 |
||||
|
MoxSy/NaY‐resulf |
Mo–S |
4.1±0.7 |
2.42±0.01 |
19 997 |
0.2±2.1 |
6.4±1.3 |
0.023 |
|
Mo–Mo |
1.0±1.2 |
2.76±0.03 |
8.2±6.7 |
||||
|
Nitrogenase FeMo‐cofactor |
Mo–S |
3[a,b] |
2.34[a], 2.32[b] |
|
|
|
|
|
Mo–Fe |
3[a,b] |
2.70[a], 2.61[b] |
Figure 3.

DFT‐optimized Mo2S4 (cis) and Mo4S4 clusters. The depicted clusters were optimized with spin‐multiplicity of 3 for Mo2S4 and 5 for Mo4S4 using B3LYP. Varying the functional did not result in a significant change in cluster geometry (Figure S6). S: yellow, Mo: blue.
Energy dispersive X‐ray spectroscopy (EDS) mapping shows an even distribution of Mo across the zeolite particles (Figure S2), proving that Mo and S are not enriched at the outer surface of the crystallites. This indicates that Mo is initially evenly distributed and remains locally anchored as sulfide clusters with two different nuclearities. The decrease in zeolite micropore volume with increasing Mo loading also supports this conclusion (Figure S3). The absence of any larger particles in the high‐angle‐annular dark field‐transmission electron microscopy (HAADF‐TEM; Figure S2) showed further that the di‐ and tetranuclear clusters are the predominant, if not the only, form of MoxSy. X‐ray diffraction patterns of the MoxSy‐containing samples and the parent NaY zeolite show a change in the relative intensities of several diffraction peaks (Figure S4), attributed to a redistribution of Na+ cations within the zeolite. [10] This indicates a slight preference of the location of the TMS clusters, requiring, however, additional analysis.
The hypothesized structures of Mo2S4 and Mo4S4 clusters were optimized using DFT and the results were compared against the experimental data (EXAFS). Interestingly, variations in the number of unpaired electrons in the Mo d‐orbitals correlated with the Mo−Mo bond distances, while the Mo‐S interatomic distances were insensitive to these changes (Figure 2).
Figure 2.

Average Mo–S (dMo‐S) and Mo–Mo (dMo‐Mo) interatomic distances, as well as the relative Gibbs free energies at 473 K (ΔG #) of Mo2S4 (left) in cis (red) and trans (green) configurations, and Mo4S4 (right) clusters as a function of spin‐multiplicity as calculated by DFT using B3LYP, PBE0, and TPSSh functionals. Experimentally observed dMo‐Mo and dMo‐S estimated from the EXAFS of MoxSy/NaY‐sulf/red catalysts are shown as dashed lines.
The DFT‐computed dMo‐Mo (Table S3) obtained for the thermodynamically most stable configurations (spin‐multiplicity of 3 for Mo2S4 and 5 for Mo4S4) match excellently with the values obtained from EXAFS (Table 1). The computed dMo‐S however appear to be significantly lower than those observed experimentally, which we attribute to the fact that geometry optimization was performed in gas phase, while for the zeolite‐encaged clusters, the terminal S atoms are likely to interact with sodium cations in the zeolite, which is expected to elongate the bonds. As these interactions could also lead to charge transfer to/from clusters, we investigated the influence of positive/negative charge on the optimized geometries (Figure S5). The calculations indicate that the structural parameters of these clusters are influenced more by the spin‐multiplicity than by the net charge on the clusters. Based on computed Gibbs free energies (Figure 2 and Tables S1 and S2), the lowest‐energy structures have a spin‐multiplicity of 3 (two unpaired electrons) and 5 (four unpaired electrons) for Mo2S4 and Mo4S4 (Figure 3), respectively. For Mo2S4, the cis configuration was found to be more stable and is further examined.
As DFT calculations correspond to one unpaired electron per Mo for both clusters, the presence of unpaired electrons on Mo was also deduced from the EPR measurements (Figure 4 left). The EPR spectra show an intense central line with g‐values ≈2, in close agreement with the g‐values reported for unpaired electrons in Mo species of different formal oxidation states in nitrogenase, nitrate reductase, and sulfur‐bridged Mo dimer clusters. [11] Although EPR signals with g ≈2 are commonly assigned to S= systems, these signals may also be interpreted as Ms ±1 transitions of systems with higher spin‐multiplicities, e.g., cis‐Mo2S4 (spin‐multiplicity=3) and Mo4S4 (spin‐multiplicity=5), with a large zero field splitting. [11a] Due to the lack of spin quantification, an in‐depth electronic spin analysis of MoxSy clusters proposed in this work is presently not achievable. It must also be noted that a mixture of clusters with different spin‐multiplicities may be present as the DFT‐computed Gibbs free energy difference between systems with slightly different multiplicities is relatively small (Figure 2 and Table S1 and S2).
Figure 4.

EPR spectra of MoxSy/NaY‐sulf/red catalysts (left) and the isosurface (0.02 a.u.) of the difference in alpha and beta electron densities (right) illustrating the location of unpaired electrons on cis‐ Mo2S4 (spin‐multiplicity=3) and Mo4S4 (spin‐multiplicity=5) clusters computed using DFT(B3LYP).
The DFT calculations unambiguously support our finding that the unpaired electrons are indeed located on the Mo atoms of both MoxSy clusters (Figure 4, right and Figure S6). In this regard, it is important to note that ionic clusters would result in formal Mo oxidation states of +4/+2 (assuming neutral Mo2S4/Mo4S4 clusters) which could not possess single unpaired electrons due to their even number of total valence electrons. However, the Mo−S bonds in these nanoclusters are likely to be covalent in character, which is supported by Hirshfeld/Mulliken population analysis and Mayer bond orders computed using DFT (Tables S4 and S5).
Further confirmation of the hypothesized structures of NaY encapsulated MoxSy clusters was deduced from Mo Kα high energy resolution fluorescence detected X‐ray absorption near edge structure (HERFD‐XANES) and Mo Kβ valence‐to‐core (VtC) XES. The VtC XES spectra of MoxSy/NaY‐sulf/red catalysts are in close agreement with the simulated spectra of the optimized Mo2S4 and Mo4S4 structures (Figure S7 and Table S6) validating the structures suggested in this work. In addition, HERFD‐XANES shows a shift towards lower absorption energies for the reduced catalyst supporting the proposed reduction of Mo centers in a pure H2 atmosphere (Figure S10).
Interestingly, when subjecting the two clusters catalysts to a stream of ethene and H2, no activity was observed at the very beginning, but both catalysts gained activity and reached a steady‐state over a time span of ≈30 h (Figure 5). Elemental analysis of the spent MoxSy/NaY‐sulf sample showed a loss of sulfur that corresponded to approximately one S per cluster. Thus, we hypothesize that partial sulfur loss from the fully sulfided Mo2S4 cluster may account for the generation of true active sites (S‐vacancies) while the original clusters are inactive. Given the high reduction temperature (673 K in pure H2), further reduction and sulfur loss is rather unlikely for the MoxSy/NaY‐red sample at the reaction temperature of 473 K and the induction period could be caused by restructuring.
Figure 5.

Steady‐state ethane formation rates (top) at 473 K for cluster catalysts with different loadings and time‐on‐stream behavior (bottom) of representative MoxSy/NaY‐sulf/red catalysts and MoS2/NaMFI.
While it would also be very important to understand a potential response of the Mo spin states to its local coordination environment, this is to be further investigated by in situ spectroscopy (EPR and XAS in particular) that monitors the dynamic evolution of the structure and chemical compositions of the active sites at reaction conditions.
For MoxSy/NaY‐sulf/red catalysts, a linear increase of the steady‐state ethane formation rate (per gram of catalyst) was observed with an increasing loading of clusters (Figure 5). The parent NaY zeolite itself (no EFAl species or Brønsted acid sites; Figures S1 and S11) did not exhibit hydrogenation activity. Therefore, we conclude that the measured activity stems solely from MoxSy clusters that are homogeneous in nature. Surprisingly, the linear rate increase was identical for di‐ and tetramers indicating that each cluster forms the same number of equally active sites.
The cluster catalysts showed stable steady‐state conversion rates (for at least 7 days), allowing to conclude that the active sulfide sites hosted in the zeolite cages remained stable, in contrast to previous studies that either lacked evaluation of the stability metric or clearly noted deactivation/degradation of the active structures.[ 7a , 7b , 8 ] A traditional MoS2/NaMFI catalyst that featured extended slabs, however, deactivated markedly after reaching the maximum activity (Figure 5). The NaMFI zeolite used as a support is free of Brønsted acid sites and did not show any activity under the probed conditions. We, therefore, conclude that deactivation results from degradation of the MoS2 phase without supply of sulfur in the reactant stream.
In summary, we have shown that di‐ and tetrameric MoxSy clusters can be stabilized in a homogeneous form by zeolite Na‐FAU. The active clusters are homogeneously distributed in the zeolite and are essentially homotopic. The specific catalytic activity of these clusters for ethene hydrogenation is identical. The tetrameric cluster is structurally similar to the Mo site of the FeMo‐cofactor in nitrogenase. DFT‐based optimization of the cluster geometry and free energy calculations predict that both clusters contain a single unpaired electron at each Mo atom. While the intrinsic catalytic activity is similar to those of a conventional supported MoS2 catalyst, the latter deactivates markedly during time on stream while both the di‐and tetrameric MoxSy cluster‐based catalysts are stable for days of operation. Thus, the zeolite‐supported MoxSy cluster catalysts are a promising new class of robust, bio‐inspired hydrogenation catalysts that create exciting opportunities with respect to chemical and structural variability for catalysis.
Conflict of interest
The authors declare no conflict of interest.
Supporting information
As a service to our authors and readers, this journal provides supporting information supplied by the authors. Such materials are peer reviewed and may be re‐organized for online delivery, but are not copy‐edited or typeset. Technical support issues arising from supporting information (other than missing files) should be addressed to the authors.
Supplementary
Acknowledgements
This work was funded by the Chevron Energy Technology Company. The authors especially thank Dr. A. Kuperman and Dr. A. Brait (Chevron), and Prof. Takeshi Kubota (Shimane University, Japan) for fruitful discussions. Conceptual work and structural determinations were supported by the U.S. Department of Energy (DOE), Office of Science, Office of Basic Energy Sciences (BES), Division of Chemical Sciences, Geosciences and Biosciences (Transdisciplinary Approaches to Realize Novel Catalytic Pathways to Energy Carriers, FWP 47319). Portions of the experiments were performed at the William R. Environmental Molecular Science Laboratory (EMSL), a national scientific user facility sponsored by the DOE Office of Biological and Environmental Research located at Pacific Northwest National Laboratory (PNNL). PNNL is a multiprogram national laboratory operated for DOE by Battelle. The authors gratefully acknowledge the Leibniz Supercomputing Center for funding this project by providing computing time on their Linux‐Cluster. The X‐ray absorption and emission spectroscopy measurements were performed on beamline ID26 at the European Synchrotron Radiation Facility (ESRF), Grenoble, France (Proposal CH‐5641). We are grateful to Dr. Pieter Glatzel at the ESRF for his assistance. The authors also want to thank Dr. O. Storcheva (EPR spectroscopy), T. Schachtl and M. Aigner (NMR spectroscopy), and C. Gross (syntheses and reactions) for their help. Open access funding enabled and organized by Projekt DEAL.
R. Weindl, R. Khare, L. Kovarik, A. Jentys, K. Reuter, H. Shi, J. A. Lercher, Angew. Chem. Int. Ed. 2021, 60, 9301.
Contributor Information
Prof. Hui Shi, Email: shihui@yzu.edu.cn.
Prof. Johannes A. Lercher, Email: Johannes.lercher@ch.tum.de.
References
- 1.
- 1a. Howard J. B., Rees D. C., Chem. Rev. 1996, 96, 2965–2982; [DOI] [PubMed] [Google Scholar]
- 1b. Burgess B. K., Lowe D. J., Chem. Rev. 1996, 96, 2983–3011; [DOI] [PubMed] [Google Scholar]
- 1c. Kowalska J., DeBeer S., Biochim. Biophys. Acta Mol. Cell Res. 2015, 1853, 1406–1415; [DOI] [PubMed] [Google Scholar]
- 1d. Lancaster K. M., Roemelt M., Ettenhuber P., Hu Y., Ribbe M. W., Neese F., Bergmann U., DeBeer S., Science 2011, 334, 974–977; [DOI] [PMC free article] [PubMed] [Google Scholar]
- 1e. Bjornsson R., Neese F., Schrock R. R., Einsle O., DeBeer S., J. Biol. Inorg. Chem. 2015, 20, 447–460; [DOI] [PMC free article] [PubMed] [Google Scholar]
- 1f. Bjornsson R., Lima F. A., Spatzal T., Weyhermüller T., Glatzel P., Bill E., Einsle O., Neese F., DeBeer S., Chem. Sci. 2014, 5, 3096–3103; [Google Scholar]
- 1g. Einsle O., Tezcan F. A., Andrade S. L. A., Schmid B., Yoshida M., Howard J. B., Rees D. C., Science 2002, 297, 1696–1700; [DOI] [PubMed] [Google Scholar]
- 1h. George S. J., Barney B. M., Mitra D., Igarashi R. Y., Guo Y., Dean D. R., Cramer S. P., Seefeldt L. C., J. Inorg. Biochem. 2012, 112, 85–92; [DOI] [PMC free article] [PubMed] [Google Scholar]
- 1i. George S. J., Hernandez J. A., Jimenez-Vicente E., Echavarri-Erasun C., Rubio L. M., Chem. Commun. 2016, 52, 11811–11814. [DOI] [PMC free article] [PubMed] [Google Scholar]
- 2.
- 2a. Grilc M., Likozar B., Levec J., Appl. Catal. B 2014, 150–151, 275–287; [Google Scholar]
- 2b. Liu G., Robertson A. W., Li M. M.-J., Kuo W. C. H., Darby M. T., Muhieddine M. H., Lin Y.-C., Suenaga K., Stamatakis M., Warner J. H., Tsang S. C. E., Nat. Chem. 2017, 9, 810–816; [DOI] [PubMed] [Google Scholar]
- 2c. Eijsbouts S., Mayo S. W., Fujita K., Appl. Catal. A 2007, 322, 58–66. [Google Scholar]
- 3.
- 3a. Tran P. D., Nguyen M., Pramana S. S., Bhattacharjee A., Chiam S. Y., Fize J., Field M. J., Artero V., Wong L. H., Loo J., Barber J., Energy Environ. Sci. 2012, 5, 8912; [Google Scholar]
- 3b. Tran P. D., Tran T. V., Orio M., Torelli S., Truong Q. D., Nayuki K., Sasaki Y., Chiam S. Y., Yi R., Honma I., Barber J., Artero V., Nat. Mater. 2016, 15, 640–646; [DOI] [PMC free article] [PubMed] [Google Scholar]
- 3c. Lu A.-Y., Yang X., Tseng C.-C., Min S., Lin S.-H., Hsu C.-L., Li H., Idriss H., Kuo J.-L., Huang K.-W., Li L.-J., Small 2016, 12, 5530–5537; [DOI] [PubMed] [Google Scholar]
- 3d. Voiry D., Fullon R., Yang J., de Carvalho Castro e Silva C., Kappera R., Bozkurt I., Kaplan D., Lagos M. J., Batson P. E., Gupta G., Mohite A. D., Dong L., Er D., Shenoy V. B., Asefa T., Chhowalla M., Nat. Mater. 2016, 15, 1003–1009; [DOI] [PubMed] [Google Scholar]
- 3e. Seo B., Joo S. H., Nano Convergence 2017, 4, 19. [DOI] [PMC free article] [PubMed] [Google Scholar]
- 4.
- 4a. Helveg S., Lauritsen J. V., Laegsgaard E., Stensgaard I., Norskov J. K., Clausen B. S., Topsoe H., Besenbacher F., Phys. Rev. Lett. 2000, 84, 951–954; [DOI] [PubMed] [Google Scholar]
- 4b. Topsoe N.-Y., Topsoe H., J. Catal. 1983, 84, 386–401. [Google Scholar]
- 5.
- 5a. Wolff T. E., Berg J. M., Warrick K. O. H., Holm R. H., J. Am. Chem. Soc. 1978, 100, 4630–4632; [Google Scholar]
- 5b. Seino H., Hidai M., Chem. Sci. 2011, 2, 847. [Google Scholar]
- 6.
- 6a. Coucouvanis D., Demadis K. D., Malinak S. M., Mosier P. E., Tyson M. A., Laughlin L. J., J. Mol. Catal. A 1996, 107, 123–135; [Google Scholar]
- 6b. Coucouvanis D., Mosier P. E., Demadis K. D., Patton S., Malinak S. M., Kim C. G., Tyson M. A., J. Am. Chem. Soc. 1993, 115, 12193–12194; [Google Scholar]
- 6c. Demadis K. D., Malinak S. M., Coucouvanis D., Inorg. Chem. 1996, 35, 4038–4046; [DOI] [PubMed] [Google Scholar]
- 6d. Malinak S. M., Simeonov A. M., Mosier P. E., McKenna C. E., Coucouvanis D., J. Am. Chem. Soc. 1997, 119, 1662–1667; [Google Scholar]
- 6e. Herbst K., Monari M., Brorson M., Inorg. Chem. 2002, 41, 1336–1338; [DOI] [PubMed] [Google Scholar]
- 6f. Laughlin L. J., Coucouvanis D., J. Am. Chem. Soc. 1995, 117, 3118–3125. [Google Scholar]
- 7.
- 7a. Taniguchi M., Imamura D., Ishige H., Ishii Y., Murata T., Hidai M., Tatsumi T., J. Catal. 1999, 187, 139–150; [Google Scholar]
- 7b. Hédoire C.-E., Cadot E., Villain F., Davidson A., Louis C., Breysse M., Appl. Catal. A 2006, 306, 165–174; [Google Scholar]
- 7c. Müller A., Sarkar S., Bhattacharyya R. G., Pohl S., Dartmann M., Angew. Chem. Int. Ed. Engl. 1978, 17, 535; [Google Scholar]; Angew. Chem. 1978, 90, 567; [Google Scholar]
- 7d. Shibahara T., Yamasaki M., Sakane G., Minami K., Yabuki T., Ichimura A., Inorg. Chem. 1992, 31, 640–647. [Google Scholar]
- 8. Hensen E. J. M., van Veen J. A. R., Catal. Today 2003, 86, 87–109. [Google Scholar]
- 9.
- 9a. Kadono T., Chatani H., Kubota T., Okamoto Y., Microporous Mesoporous Mater. 2007, 101, 191–199; [Google Scholar]
- 9b. Kadono T., Kubota T., Chatani H., Kawabata T., Okamoto Y., Stud. Surf. Sci. Catal. 2006, 162, 849–856; [Google Scholar]
- 9c. Okamoto Y., Bull. Chem. Soc. Jpn. 2014, 87, 20–58. [Google Scholar]
- 10.
- 10a. Okamoto Y., Katsuyama H., Yoshida K., Nakai K., Matsuo M., Sakamoto Y., Yu J., Terasaki O., J. Chem. Soc. Faraday Trans. 1996, 92, 4647–4656; [Google Scholar]
- 10b. Salama T. M., Othman I., Sirag M., El-Shobaky G. A., Microporous Mesoporous Mater. 2006, 95, 312–320. [Google Scholar]
- 11.
- 11a. Van Stappen C., Decamps L., G. E. Cutsail III , Bjornsson R., Henthorn J. T., Birrell J. A., DeBeer S., Chem. Rev. 2020, 120, 5005–5081; [DOI] [PMC free article] [PubMed] [Google Scholar]
- 11b. Biaso F., Burlat B., Guigliarelli B., Inorg. Chem. 2012, 51, 3409–3419; [DOI] [PubMed] [Google Scholar]
- 11c. Casewit C. J., DuBois M. R., Inorg. Chem. 1986, 25, 74–80. [Google Scholar]
Associated Data
This section collects any data citations, data availability statements, or supplementary materials included in this article.
Supplementary Materials
As a service to our authors and readers, this journal provides supporting information supplied by the authors. Such materials are peer reviewed and may be re‐organized for online delivery, but are not copy‐edited or typeset. Technical support issues arising from supporting information (other than missing files) should be addressed to the authors.
Supplementary
