Supported Rh nanoparticles obtained by reduction in hydrogen of severely calcined Rh/Mg/Al hydrotalcite-type (HT) phases have been characterized by FT-IR spectroscopy of adsorbed CO [both at room temperature (r.t.) and nominal liquid nitrogen temperature] and Transmission Electron Microscopy (TEM). The effect of reducing temperature has been investigated, showing that Rh crystal size increases from 1.4?nm to 1.8?nm when the reduction temperature increases from 750°C to 950°C. The crystal growth favours the formation of bridged CO species and linear monocarbonyl species with respect to gem-dicarbonyl species; when CO adsorbs at r.t., CO disproportionation occurs on Rh and it accompanies the formation of (CO)2. The role of interlayer anions in the HT precursors to affect the properties of the final materials has been also investigated considering samples prepared from silicate-instead of carbonate-containing precursors. In this case, formation of (CO)2 and CO disproportionation do not occur, and this evidence is discussed in terms of support effect. 1. Introduction Hydrotalcites or layered double hydroxides (LDH’s) belong to a large class of natural and synthetic anionic clays. Although they are less diffuse in nature than cationic clays, they can be easily synthesized [1]. Hydrotalcites-type (HT) compounds have the general formula: The cations are present in a layer with brucite-type structure [Mg(OH)2], in which part of Mg2+ is replaced by Al3+ and, as a consequence, the positive additional charge of the cations is balanced by the insertion of anions between layers. Usually carbonates are used as anions, even if samples with silicates have shown higher thermal and textural stability [2]. The mixed oxides obtained after calcination of HT phases at temperature above 500°C are very useful for a wide range of applications like antiacids, anion exchanger, adsorbents, catalysts, and catalyst supports because of their undeniable advantages as high surface area and structural stability [3]. A further increase of the calcination temperature above 750°C gives rise to the segregation of the stoichiometric spinel phase and the formation of less defective MgO-type phase, giving rise to stable supports or catalysts for high temperature processes. In particular, the modification of the catalytic properties is possible by the substitution of part of Mg with other bivalent cation as Ni, Pt, Pd, Co, and/or part of Al ions with Rh, Fe, Cr obtaining a high variety of formulation [3, 4]. The structure and surface properties of Mg-Al HT phases and of the resulting mixed
References
[1]
S. Casenave, H. Martinez, C. Guimon et al., “Acid-base properties of Mg-Ni-Al mixed oxides using LDH as precursors,” Thermochimica Acta, vol. 379, no. 1-2, pp. 85–93, 2001.
[2]
S. Albertazzi, F. Basile, P. Benito et al., “Effect of silicates on the structure of Ni-containing catalysts obtained from hydrotalcite-type precursors,” Catalysis Today, vol. 128, no. 3-4, pp. 258–263, 2007.
[3]
F. Cavani, F. Trifirò, and A. Vaccari, “Hydrotalcite-type anionic clays: preparation, properties and applications,” Catalysis Today, vol. 11, no. 2, pp. 173–301, 1991.
[4]
F. Basile, P. Benito, G. Fornasari, and A. Vaccari, “Hydrotalcite-type precursors of active catalysts for hydrogen production,” Applied Clay Science, vol. 48, no. 1-2, pp. 250–259, 2010.
[5]
F. Basile, G. Fornasari, M. Gazzano, A. Kiennemann, and A. Vaccari, “Preparation and characterisation of a stable Rh catalyst for the partial oxidation of methane,” Journal of Catalysis, vol. 217, no. 2, pp. 245–252, 2003.
[6]
J. T. Yates Jr., T. M. Duncan, and R. W. Vaughan, “Infrared spectra of chemisorbed CO on Rh,” Journal of Chemical Physics, vol. 71, 3908 pages, 1979.
[7]
A. Erd?helyi and F. Solymosi, “Effects of the support on the adsorption and dissociation of CO and on the reactivity of surface carbon on Rh catalysts,” Journal of Catalysis, vol. 84, no. 2, pp. 446–460, 1983.
[8]
S. Trautmann and M. Baerns, “Infrared Spectroscopic Studies of CO Adsorption on Rhodium Supported by SiO2, Al2O3, and TiO2,” Journal of Catalysis, vol. 150, no. 2, pp. 335–344, 1994.
[9]
L. Kundakovic, D. R. Mullins, and S. H. Overbury, “Adsorption and reaction of H2O and CO on oxidized and reduced Rh/CeOx(111) surfaces,” Surface Science, vol. 457, no. 1, pp. 51–62, 2000.
[10]
E. Finocchio, G. Buscai, P. Forzatti, G. Groppi, and A. Beretta, “State of supported rhodium nanoparticles for methane catalytic partial oxidation (CPO); FT-IR studies,” Langmuir, vol. 23, no. 20, pp. 10419–10428, 2007.
[11]
K. Hadjiivanov, E. Ivanova, L. Dimitrov, and H. Kn?zinger, “FTIR spectroscopic study of CO adsorption on Rh-ZSM-5: detection of Rh +-CO species,” Journal of Molecular Structure, vol. 661-662, no. 1–3, pp. 459–463, 2003.
[12]
F. Basile, G. Fornasari, M. Gazzano, and A. Vaccari, “Rh, Ru and Ir catalysts obtained by HT precursors: effect of the thermal evolution and composition on the material structure and use,” Journal of Materials Chemistry, vol. 12, no. 11, pp. 3296–3303, 2002.
[13]
F. Basile, P. Benito, G. Fornasari et al., “Ni-catalysts obtained from silicate intercalated HTlcs active in the catalytic partial oxidation of methane: influence of the silicate content,” Catalysis Today, vol. 142, no. 1-2, pp. 78–84, 2009.
[14]
T. Chafik, D. I. Kondarides, and X. E. Verykios, “Catalytic reduction of NO by CO over rhodium catalysts: 1. Adsorption and displacement characteristics Investigated by in situ FTIR and transient-MS techniques,” Journal of Catalysis, vol. 190, no. 2, pp. 446–459, 2000.
[15]
D. I. Kondarides, T. Chafik, and X. E. Verykios, “Catalytic reduction of NO by CO over Rhodium catalysts: 2. Effect of oxygen on the nature, population, and reactivity of surface species formed under reaction conditions,” Journal of Catalysis, vol. 191, no. 1, pp. 147–164, 2000.
[16]
H. Miessner, D. Gutschick, H. Ewald, and H. Müller, “The influence of support on the geminal dicarbonyl species RhI(CO)2 on supported rhodium catalysts: an IR spectroscopic study,” Journal of Molecular Catalysis, vol. 36, no. 3, pp. 359–373, 1986.
[17]
A. M. Turek, I. E. Wachs, and E. DeCanio, “Acidic properties of alumina-supported metal oxide catalysts: an infrared spectroscopy study,” Journal of Physical Chemistry, vol. 96, no. 12, pp. 5000–5007, 1992.
[18]
A. A. Davydov, M. L. Shepot’ko, and A. A. Budneva, “Study of the state of transition-metal cations on the catalyst surface by IR spectroscopy using adsorbed probe-molecules (CO, NO): X. Identification of the state of copper on the surface of Cu/SiO2,” Kinetics and Catalysis, vol. 35, p. 272, 1994.
[19]
J. C. Lavalley, “Infrared spectrometric studies of the surface basicity of metal oxides and zeolites using adsorbed probe molecules,” Catalysis Today, vol. 27, no. 3-4, pp. 377–401, 1996.
[20]
G. Bergeret, P. Gallezot, P. Gelin et al., “CO-induced disintegration of rhodium aggregates supported in zeolites: in situ synthesis of rhodium carbonyl clusters,” Journal of Catalysis, vol. 104, no. 2, pp. 279–287, 1987.
[21]
F. Solymosi, M. Pásztor, and G. Rákhely, “Infrared studies of the effects of promoters on CO-induced structural changes in Rh,” Journal of Catalysis, vol. 110, no. 2, pp. 413–415, 1988.
[22]
H. F. J. Van't Blik, J. B. A. D. Van Zon, T. Hulzinga, J. C. Vis, D. C. Koningsberger, and R. Prins, “An extended X-ray absorption fine structure spectroscopy study of a highly dispersed Rh/Al2O3 catalyst: the influence of CO chemisorption on the topology of rhodium,” Journal of Physical Chemistry, vol. 87, no. 13, pp. 2264–2267, 1983.
[23]
J. Raskó and J. Bontovics, “FTIR study of the rearrangement of adsorbed CO species on Al2O3-supported rhodium catalysts,” Catalysis Letters, vol. 58, no. 1, pp. 27–32, 1999.
[24]
M. Primet, “Infrared study of CO chemisorption on zeolite and alumina supported rhodium,” Journal of the Chemical Society, Faraday Transactions 1, vol. 74, pp. 2570–2580, 1978.
[25]
P. Basu, D. Panayotov, and J. T. Yates, “Rhodium-carbon monoxide surface chemistry: the involvement of surface hydroxyl groups on Al2O3 and SiO2 supports,” Journal of the American Chemical Society, vol. 110, no. 7, pp. 2074–2081, 1988.
[26]
A. Bossi, G. Carnisio, F. Garmassi, G. Giunchi, G. Petrini, and L. Zanderighi, “Isotopic equilibration of carbon monoxide catalyzed by supported ruthenium,” Journal of Catalysis, vol. 65, p. 16, 1980.
[27]
K. L. Zhang, A. Kladi, and X. E. Verykios, “Structural alterations of highly dispersed Rh/TiO2 catalyst upon CO adsorption and desorption investigated by infrared spectroscopy,” Journal of Molecular Catalysis, vol. 89, no. 1-2, pp. 229–246, 1994.
[28]
C. A. Rice, S. D. Worley, C. W. Curtis, J. A. Guin, and A. R. Tarrer, “The oxidation state of dispersed Rh on AI2O3,” The Journal of Chemical Physics, vol. 74, no. 11, pp. 6487–6497, 1981.
[29]
G. Lafaye, C. Mihut, C. Especel, P. Marécot, and M. D. Amiridis, “FTIR studies of CO adsorption on Rh-Ge/Al2O3 catalysts prepared by surface redox reactions,” Langmuir, vol. 20, no. 24, pp. 10612–10616, 2004.