6 research outputs found

    A new molecular pathway allows the chemoselective reduction of nitroaromatics on non-noble metal catalysts

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    [EN] At difference with noble metals, the oxophylic character of non-noble metals strongly facilitates the rupture of the N-O bonds in nitrobenzene, yielding nitrosobenzene as primary reaction intermediate. By combining periodic DFT calculations and kinetic studies, a direct pathway involving successive dissociation of N-O bonds followed by two hydrogenation steps, Ph-NO2 -> Ph-NO -> Ph-N -> Ph-NH -> Ph-NH2, has been found as most favorable on Ni catalysts. The rate determining step of the global process is the hydrogen transfer to adsorbed Ph-N intermediate. The catalyst surface becomes partly oxidized during reaction, which favors the vertical adsorption of the nitroaromatic compounds and enhances selectivity, while total surface oxidation leads to catalyst deactivation. It is proposed that both catalytic activity and selectivity of Ni and, possibly, other non-noble metals can be tuned by controlling the degree of oxidation of the metal surface. (C) 2018 Elsevier Inc. All rights reserved. KeywordsThis work has been supported by the Spanish Government through "Severo Ochoa Program" (SEV-2016-0683) and by Generalitat Valenciana through AICO/2017/153 Project. Red Espanola de Supercomputacion (RES) and Centre de Calcul de la Universitat de Valencia are gratefully acknowledged for computational resources and technical support. The authors also thank the Microscopy Service of UPV for kind help on measurements. R. M. acknowledges "La Caixa - Severo Ochoa" International PhD Fellowships (call 2015). L. L. thanks ITQ for providing a PhD scolarship.Millán-Cabrera, R.; Liu, L.; Boronat Zaragoza, M.; Corma Canós, A. (2018). A new molecular pathway allows the chemoselective reduction of nitroaromatics on non-noble metal catalysts. Journal of Catalysis. 364:19-30. https://doi.org/10.1016/j.jcat.2018.05.004193036

    Spectroscopic Evidence and Density Functional Theory (DFT) Analysis of Low-Temperature Oxidation of Cu+ to Cu2+NOx in Cu-CHA Catalysts: Implications for the SCR-NOx Reaction Mechanism

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    "This document is the Accepted Manuscript version of a Published Work that appeared in final form in ACS Catalysis, copyright © American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see https://doi.org/10.1021/acscatal.8b04717."[EN] Despite the intense investigation on the NH3-SCR-NOx reaction mechanism catalyzed by small pore Cu-CHA zeolites, neither the rate-determining step of the process nor the exact nature of the active sites under reaction conditions are clearly established. In this work, in situ EPR and IR techniques combined with DFT calculations are applied to the study of the oxidation half-cycle of the NH3-SCR-NOx reaction on Cu-SSZ-13 and Cu-SAPO-34 catalysts. EPR and IR spectroscopies unambiguously show that Cu+ is oxidized to Cu2+ at room temperature in the presence of the reaction mixture (NO, O-2, and NH3) or NO and O-2, producing adsorbed NO2, nitrites, and nitrates. Several pathways are proposed from DFT calculations to oxidize Cu+ cations placed in the plane of the 6R ring units of SSZ-13 and SAPO-34 to Cu2+, either by NO2 alone or by a mixture of NO and O-2, with activation energy barriers lower than 70 kJ mol(-1). The results reported here demonstrate that a reaction mechanism invoking the formation of nitrate/nitrite intermediates on copper cations attached to the zeolite framework can be operational in the low-temperature region (T < 350 degrees C). Moreover, different intermediates, nitrites versus nitrates, are preferentially stabilized, depending on the catalyst composition, silicoaluminophosphate vs aluminosilicate.This work was supported by the Spanish Government through "Severo Ochoa Program" (Nos. SEV 2012-0267; SEV-2016-0683), No. MAT2015-71261-R, and No. CTQ2015-68951-C3-1-R, and by the European Union through No. ERC-AdG-2014-671093 (SynCatMatch). Red Espanola de Supercomputacion (RES) and Centre de Calcul de la Universitat de Valencia are gratefully acknowledged for computational resources and technical support. R.M. acknowledges "La Caixa-Severo Ochoa" International PhD Fellowships (call 2015).Moreno-González, M.; Millán-Cabrera, R.; Concepción Heydorn, P.; Blasco Lanzuela, T.; Boronat Zaragoza, M. (2019). Spectroscopic Evidence and Density Functional Theory (DFT) Analysis of Low-Temperature Oxidation of Cu+ to Cu2+NOx in Cu-CHA Catalysts: Implications for the SCR-NOx Reaction Mechanism. ACS Catalysis. 9(4):2725-2738. https://doi.org/10.1021/acscatal.8b04717S272527389

    Impact of Zeolite Framework Composition and Flexibility on Methanol-To-Olefins Selectivity: Confinement or Diffusion?

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    This is the peer reviewed version of the following article: P. Ferri, C. Li, R. Millán, J. Martínez-Triguero, M. Moliner, M. Boronat, A. Corma, Angew. Chem. Int. Ed. 2020, 59, 19708, which has been published in final form at https://doi.org/10.1002/anie.202007609. This article may be used for non-commercial purposes in accordance with Wiley Terms and Conditions for Self-Archiving.[EN] The methanol-to-olefins reaction catalyzed by small-pore cage-based acid zeolites and zeotypes produces a mixture of short chain olefins, whose selectivity to ethene, propene and butene varies with the cavity architecture and with the framework composition. The product distribution of aluminosilicates and silicoaluminophosphates with the CHA and AEI structures (H-SSZ-13, H-SAPO-34, H-SSZ-39 and H-SAPO-18) has been experimentally determined, and the impact of acidity and framework flexibility on the stability of the key cationic intermediates involved in the mechanism and on the diffusion of the olefin products through the8rwindows of the catalysts has been evaluated by means of periodic DFT calculations and ab initio molecular dynamics simulations. The preferential stabilization by confinement of fully methylated hydrocarbon pool intermediates favoring the paring pathway is the main factor controlling the final olefin product distribution.This work has been supported by the European Union through ERC-AdG-2014-671093 (SynCatMatch), Spanish Government through "Severo Ochoa" (SEV-2016-0683, MINECO), MAT2017-82288-C2-1-P (AEI/FEDER, UE) and RTI2018-101033-B-I00 (MCIU/AEI/FEDER, UE), and by Generalitat Valenciana through AICO/2019/060. The Electron Microscopy Service of the UPV is acknowledged for their help in sample characterization. Red Espanola de Supercomputacion (RES) and Servei d'Informatica de la Universitat de Valencia (SIUV) are acknowledged for computational resources and technical support. P.F. and R.M. thank ITQ for their contracts. C.L. acknowledges China Scholarship Council (CSC) for a Ph.D fellowship.Ferri-Vicedo, P.; Li, C.; Millán-Cabrera, R.; Martínez-Triguero, J.; Moliner Marin, M.; Boronat Zaragoza, M.; Corma Canós, A. (2020). Impact of Zeolite Framework Composition and Flexibility on Methanol-To-Olefins Selectivity: Confinement or Diffusion?. Angewandte Chemie International Edition. 59(44):19708-19715. https://doi.org/10.1002/anie.202007609S19708197155944Olah, G. A. (2005). Beyond Oil and Gas: The Methanol Economy. Angewandte Chemie International Edition, 44(18), 2636-2639. doi:10.1002/anie.200462121Olah, G. A. (2005). Jenseits von Öl und Gas: die Methanolwirtschaft. Angewandte Chemie, 117(18), 2692-2696. doi:10.1002/ange.200462121Tian, P., Wei, Y., Ye, M., & Liu, Z. (2015). Methanol to Olefins (MTO): From Fundamentals to Commercialization. ACS Catalysis, 5(3), 1922-1938. doi:10.1021/acscatal.5b00007Haw, J. F., Song, W., Marcus, D. M., & Nicholas, J. B. (2003). The Mechanism of Methanol to Hydrocarbon Catalysis. Accounts of Chemical Research, 36(5), 317-326. doi:10.1021/ar020006oOlsbye, U., Svelle, S., Bjørgen, M., Beato, P., Janssens, T. V. W., Joensen, F., … Lillerud, K. P. (2012). Conversion of Methanol to Hydrocarbons: How Zeolite Cavity and Pore Size Controls Product Selectivity. Angewandte Chemie International Edition, 51(24), 5810-5831. doi:10.1002/anie.201103657Olsbye, U., Svelle, S., Bjørgen, M., Beato, P., Janssens, T. V. W., Joensen, F., … Lillerud, K. P. (2012). Umwandlung von Methanol in Kohlenwasserstoffe: Wie Zeolith-Hohlräume und Porengröße die Produktselektivität bestimmen. Angewandte Chemie, 124(24), 5910-5933. doi:10.1002/ange.201103657Van Speybroeck, V., De Wispelaere, K., Van der Mynsbrugge, J., Vandichel, M., Hemelsoet, K., & Waroquier, M. (2014). First principle chemical kinetics in zeolites: the methanol-to-olefin process as a case study. Chem. Soc. Rev., 43(21), 7326-7357. doi:10.1039/c4cs00146jYarulina, I., Chowdhury, A. D., Meirer, F., Weckhuysen, B. M., & Gascon, J. (2018). Recent trends and fundamental insights in the methanol-to-hydrocarbons process. Nature Catalysis, 1(6), 398-411. doi:10.1038/s41929-018-0078-5Moliner, M., Martínez, C., & Corma, A. (2013). Synthesis Strategies for Preparing Useful Small Pore Zeolites and Zeotypes for Gas Separations and Catalysis. Chemistry of Materials, 26(1), 246-258. doi:10.1021/cm4015095McCann, D. M., Lesthaeghe, D., Kletnieks, P. W., Guenther, D. R., Hayman, M. J., Van Speybroeck, V., … Haw, J. F. (2008). A Complete Catalytic Cycle for Supramolecular Methanol‐to‐Olefins Conversion by Linking Theory with Experiment. Angewandte Chemie International Edition, 47(28), 5179-5182. doi:10.1002/anie.200705453McCann, D. M., Lesthaeghe, D., Kletnieks, P. W., Guenther, D. R., Hayman, M. J., Van Speybroeck, V., … Haw, J. F. (2008). A Complete Catalytic Cycle for Supramolecular Methanol‐to‐Olefins Conversion by Linking Theory with Experiment. Angewandte Chemie, 120(28), 5257-5260. doi:10.1002/ange.200705453Wang, C.-M., Wang, Y.-D., Xie, Z.-K., & Liu, Z.-P. (2009). Methanol to Olefin Conversion on HSAPO-34 Zeolite from Periodic Density Functional Theory Calculations: A Complete Cycle of Side Chain Hydrocarbon Pool Mechanism. The Journal of Physical Chemistry C, 113(11), 4584-4591. doi:10.1021/jp810350xIlias, S., & Bhan, A. (2012). Mechanism of the Catalytic Conversion of Methanol to Hydrocarbons. ACS Catalysis, 3(1), 18-31. doi:10.1021/cs3006583De Wispelaere, K., Hemelsoet, K., Waroquier, M., & Van Speybroeck, V. (2013). Complete low-barrier side-chain route for olefin formation during methanol conversion in H-SAPO-34. Journal of Catalysis, 305, 76-80. doi:10.1016/j.jcat.2013.04.015Hemelsoet, K., Van der Mynsbrugge, J., De Wispelaere, K., Waroquier, M., & Van Speybroeck, V. (2013). Unraveling the Reaction Mechanisms Governing Methanol-to-Olefins Catalysis by Theory and Experiment. ChemPhysChem, 14(8), 1526-1545. doi:10.1002/cphc.201201023Li, J., Wei, Y., Chen, J., Tian, P., Su, X., Xu, S., … Liu, Z. (2011). Observation of Heptamethylbenzenium Cation over SAPO-Type Molecular Sieve DNL-6 under Real MTO Conversion Conditions. Journal of the American Chemical Society, 134(2), 836-839. doi:10.1021/ja209950xXu, S., Zheng, A., Wei, Y., Chen, J., Li, J., Chu, Y., … Liu, Z. (2013). Direct Observation of Cyclic Carbenium Ions and Their Role in the Catalytic Cycle of the Methanol-to-Olefin Reaction over Chabazite Zeolites. Angewandte Chemie International Edition, 52(44), 11564-11568. doi:10.1002/anie.201303586Xu, S., Zheng, A., Wei, Y., Chen, J., Li, J., Chu, Y., … Liu, Z. (2013). Direct Observation of Cyclic Carbenium Ions and Their Role in the Catalytic Cycle of the Methanol-to-Olefin Reaction over Chabazite Zeolites. Angewandte Chemie, 125(44), 11778-11782. doi:10.1002/ange.201303586Li, J., Wei, Y., Chen, J., Xu, S., Tian, P., Yang, X., … Liu, Z. (2014). Cavity Controls the Selectivity: Insights of Confinement Effects on MTO Reaction. ACS Catalysis, 5(2), 661-665. doi:10.1021/cs501669kZhang, W., Chen, J., Xu, S., Chu, Y., Wei, Y., Zhi, Y., … Liu, Z. (2018). Methanol to Olefins Reaction over Cavity-type Zeolite: Cavity Controls the Critical Intermediates and Product Selectivity. ACS Catalysis, 8(12), 10950-10963. doi:10.1021/acscatal.8b02164Song, W., Fu, H., & Haw, J. F. (2001). Supramolecular Origins of Product Selectivity for Methanol-to-Olefin Catalysis on HSAPO-34. Journal of the American Chemical Society, 123(20), 4749-4754. doi:10.1021/ja0041167Svelle, S., Olsbye, U., Joensen, F., & Bjørgen, M. (2007). Conversion of Methanol to Alkenes over Medium- and Large-Pore Acidic Zeolites:  Steric Manipulation of the Reaction Intermediates Governs the Ethene/Propene Product Selectivity. The Journal of Physical Chemistry C, 111(49), 17981-17984. doi:10.1021/jp077331jHwang, A., Johnson, B. A., & Bhan, A. (2019). Mechanistic study of methylbenzene dealkylation in methanol-to-olefins catalysis on HSAPO-34. Journal of Catalysis, 369, 86-94. doi:10.1016/j.jcat.2018.10.022Bhawe, Y., Moliner-Marin, M., Lunn, J. D., Liu, Y., Malek, A., & Davis, M. (2012). Effect of Cage Size on the Selective Conversion of Methanol to Light Olefins. ACS Catalysis, 2(12), 2490-2495. doi:10.1021/cs300558xKang, J. H., Walter, R., Xie, D., Davis, T., Chen, C.-Y., Davis, M. E., & Zones, S. I. (2018). Further Studies on How the Nature of Zeolite Cavities That Are Bounded by Small Pores Influences the Conversion of Methanol to Light Olefins. ChemPhysChem, 19(4), 412-419. doi:10.1002/cphc.201701197Kang, J. H., Alshafei, F. H., Zones, S. I., & Davis, M. E. (2019). Cage-Defining Ring: A Molecular Sieve Structural Indicator for Light Olefin Product Distribution from the Methanol-to-Olefins Reaction. ACS Catalysis, 9(7), 6012-6019. doi:10.1021/acscatal.9b00746Li, C., Paris, C., Martínez-Triguero, J., Boronat, M., Moliner, M., & Corma, A. (2018). Synthesis of reaction‐adapted zeolites as methanol-to-olefins catalysts with mimics of reaction intermediates as organic structure‐directing agents. Nature Catalysis, 1(7), 547-554. doi:10.1038/s41929-018-0104-7Ferri, P., Li, C., Paris, C., Vidal-Moya, A., Moliner, M., Boronat, M., & Corma, A. (2019). Chemical and Structural Parameter Connecting Cavity Architecture, Confined Hydrocarbon Pool Species, and MTO Product Selectivity in Small-Pore Cage-Based Zeolites. ACS Catalysis, 9(12), 11542-11551. doi:10.1021/acscatal.9b04588Chen, J., Li, J., Yuan, C., Xu, S., Wei, Y., Wang, Q., … Liu, Z. (2014). Elucidating the olefin formation mechanism in the methanol to olefin reaction over AlPO-18 and SAPO-18. Catalysis Science & Technology, 4(9), 3268. doi:10.1039/c4cy00551aDusselier, M., Deimund, M. A., Schmidt, J. E., & Davis, M. E. (2015). Methanol-to-Olefins Catalysis with Hydrothermally Treated Zeolite SSZ-39. ACS Catalysis, 5(10), 6078-6085. doi:10.1021/acscatal.5b01577Martín, N., Li, Z., Martínez-Triguero, J., Yu, J., Moliner, M., & Corma, A. (2016). Nanocrystalline SSZ-39 zeolite as an efficient catalyst for the methanol-to-olefin (MTO) process. Chemical Communications, 52(36), 6072-6075. doi:10.1039/c5cc09719cMartínez-Franco, R., Li, Z., Martínez-Triguero, J., Moliner, M., & Corma, A. (2016). Improving the catalytic performance of SAPO-18 for the methanol-to-olefins (MTO) reaction by controlling the Si distribution and crystal size. Catalysis Science & Technology, 6(8), 2796-2806. doi:10.1039/c5cy02298cBleken, F., Bjørgen, M., Palumbo, L., Bordiga, S., Svelle, S., Lillerud, K.-P., & Olsbye, U. (2009). The Effect of Acid Strength on the Conversion of Methanol to Olefins Over Acidic Microporous Catalysts with the CHA Topology. Topics in Catalysis, 52(3), 218-228. doi:10.1007/s11244-008-9158-0Wang, C.-M., Wang, Y.-D., Du, Y.-J., Yang, G., & Xie, Z.-K. (2015). Similarities and differences between aromatic-based and olefin-based cycles in H-SAPO-34 and H-SSZ-13 for methanol-to-olefins conversion: insights from energetic span model. Catalysis Science & Technology, 5(9), 4354-4364. doi:10.1039/c5cy00483gGallego, E. M., Li, C., Paris, C., Martín, N., Martínez-Triguero, J., Boronat, M., … Corma, A. (2018). Making Nanosized CHA Zeolites with Controlled Al Distribution for Optimizing Methanol-to-Olefin Performance. Chemistry - A European Journal, 24(55), 14631-14635. doi:10.1002/chem.201803637Chen, D., Moljord, K., & Holmen, A. (2012). A methanol to olefins review: Diffusion, coke formation and deactivation on SAPO type catalysts. Microporous and Mesoporous Materials, 164, 239-250. doi:10.1016/j.micromeso.2012.06.046Wang, C., Li, B., Wang, Y., & Xie, Z. (2013). Insight into the topology effect on the diffusion of ethene and propene in zeolites: A molecular dynamics simulation study. Journal of Energy Chemistry, 22(6), 914-918. doi:10.1016/s2095-4956(14)60272-2Ghysels, A., Moors, S. L. C., Hemelsoet, K., De Wispelaere, K., Waroquier, M., Sastre, G., & Van Speybroeck, V. (2015). Shape-Selective Diffusion of Olefins in 8-Ring Solid Acid Microporous Zeolites. The Journal of Physical Chemistry C, 119(41), 23721-23734. doi:10.1021/acs.jpcc.5b06010Cnudde, P., Demuynck, R., Vandenbrande, S., Waroquier, M., Sastre, G., & Speybroeck, V. V. (2020). Light Olefin Diffusion during the MTO Process on H-SAPO-34: A Complex Interplay of Molecular Factors. Journal of the American Chemical Society, 142(13), 6007-6017. doi:10.1021/jacs.9b10249“Structure Commission of the International Zeolite Association (IZA-SC) Database of Zeolite structures ” can be found underhttp://www.iza-structure.org/databases/ n.d.Olson, D. H., Camblor, M. A., Villaescusa, L. A., & Kuehl, G. H. (2004). Light hydrocarbon sorption properties of pure silica Si-CHA and ITQ-3 and high silica ZSM-58. Microporous and Mesoporous Materials, 67(1), 27-33. doi:10.1016/j.micromeso.2003.09.025Ruthven, D. M., & Reyes, S. C. (2007). Adsorptive separation of light olefins from paraffins. Microporous and Mesoporous Materials, 104(1-3), 59-66. doi:10.1016/j.micromeso.2007.01.005Hedin, N., DeMartin, G. J., Roth, W. J., Strohmaier, K. G., & Reyes, S. C. (2008). PFG NMR self-diffusion of small hydrocarbons in high silica DDR, CHA and LTA structures. Microporous and Mesoporous Materials, 109(1-3), 327-334. doi:10.1016/j.micromeso.2007.05.007Li, Z., Martínez-Triguero, J., Concepción, P., Yu, J., & Corma, A. (2013). Methanol to olefins: activity and stability of nanosized SAPO-34 molecular sieves and control of selectivity by silicon distribution. Physical Chemistry Chemical Physics, 15(35), 14670. doi:10.1039/c3cp52247

    Extending Graph (Discrete) Derivative Descriptors to N-Tuple Atom-Relations

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    In the present manuscript, an extension of the previously defined Graph Derivative Indices (GDIs) is discussed. To achieve this objective, the concept of a hypermatrix, conceived from the calculation of the frequencies of triple and quadruple atom relations in a set of connected sub-graphs, is introduced. This set of subgraphs is generated following a predefined criterion, known as the event (S), being in this particular case the connectivity among atoms. The triple and quadruple relations frequency matrices serve as a basis for the computation of triple and quadruple discrete derivative indices, respectively. The GDIs are implemented in a computational program denominated DIVATI (acronym for DIscrete DeriVAtive Type Indices), a module of TOMOCOMD-CARDD program. Shannon‟s entropy-based variability analysis demonstrates that the GDIs show major variability than others indices used in QSAR/QSPR researches. In addition, it can be appreciated when the indices are extended over n-elements from the graph, its quality increases, principally when they are used in a combined way. QSPR modeling of the physicochemical properties Log P and Log K of the 2-furylethylenes derivatives reveals that the GDIs obtained using the tripleand quadruple matrix approaches yield superior performance to the duplex matrix approach. Moreover, the statistical parameters for models obtained with the GDI method are superior to those reported in the literature by using other methods. It can therefore be suggested that the GDI method, seem to be a promissory tool to reckon on in QSAR/QSPR studies, virtual screening of compound datasets and similarity/dissimilarity evaluations

    Mobility and reactivity of Cu+ species in Cu-CHA catalysts under NH3-SCR-NOx reaction conditions : insights from AIMD simulations

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    The mobility of the copper cations acting as active sites for the selective catalytic reduction of nitrogen oxides with ammonia in Cu-CHA catalysts varies with temperature and feed composition. Herein, the migration of [Cu(NH3)2]+ complexes between two adjacent cavities of the chabazite structure, including other reactant molecules (NO, O2, H2O, and NH3), in the initial and final cavities is investigated using ab initio molecular dynamics (AIMD) simulations combined with enhanced sampling techniques to describe hopping events from one cage to the other. We find that such diffusion is only significantly hindered by the presence of excess NH3 or NO in the initial cavity, since both reactants form with [Cu(NH3)2]+ stable intermediates which are too bulky to cross the 8-ring windows connecting the cavities. The presence of O2 modifies strongly the interaction of NO with Cu+. At low temperatures, we observe NO detachment from Cu+ and increased mobility of the [Cu(NH3)2]+ complex, while at high temperatures, NO reacts spontaneously with O2 to form NO2. The present simulations give evidence for recent experimental observations, namely, an NH3 inhibition effect on the SCR reaction at low temperatures, and transport limitations of NO and NH3 at high temperatures. Our first principle simulations mimicking operating conditions support the existence of two different reaction mechanisms operating at low and high temperatures, the former involving dimeric Cu(NH3)2-O2-Cu(NH3)2 species and the latter occurring by direct NO oxidation to NO2 in one single cavity

    Theoretical and spectroscopic evidence of the dynamic nature of copper active sites in Cu-CHA catalysts under selective catalytic reduction (NH3–SCR–NOx) conditions

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    The dynamic nature of the copper cations acting as active sites for selective catalytic reduction of nitrogen oxides with ammonia is investigated using a combined theoretical and spectroscopic approach. Ab initio molecular dynamics simulations of Cu-CHA catalysts in contact with reactants and intermediates at realistic operating conditions show that only ammonia is able to release Cu+ and Cu2+ cations from their positions coordinated to the zeolite framework, forming mobile Cu+(NH3)(2) and Cu2+(NH3)(4) complexes that migrate to the center of the cavity. Herein, we give evidence that such mobilization of copper cations modifies the vibrational fingerprint in the 800-1000 cm(-1) region of the IR spectra. Bands associated with the lattice asymmetric T-O-T vibrations are perturbed by the presence of coordinated cations, and allow one to experimentally follow the dynamic reorganization of the active sites at operating conditions
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