Oxidative steam reforming of ethanol over Ir/CeO2 catalysts: A structure sensitivity analysis

A series of Ir/CeO2 catalysts of different oxide and metallic phase dispersions was investigated by XRD, TPR, HRTEM, CO2 TPD/calorimetry, in situ DRIFT spectroscopy, and oxygen isotopic exchange techniques in order to elucidate the specific influence of catalyst morphology and structure on the oxidative steam reforming (OSR) of ethanol. Structure/texture sensitivity is demonstrated on the basis of the OSR mechanism, which involves, in order: (i) ethanol adsorption on the ceria surface, (ii) partial oxidation to acetate and surface migration of the C2 intermediates along the ceria support toward the Ir particles. (iii) cracking and further oxidation into Ir carbonyls and ceria carbonates, and (iv) hydrogen and carbon monoxide desorption from the Ir particles. Structure sensitivity is established by considering two types of sites: the ceria surface sites, which are essentially pairs of oxygen vacancies and basic OH groups, as well as interfacial sites between Ir and ceria phases, involving pairs of Ir coordinately unsaturated sites (CUSs) and the aforementioned Peripheral ceria sites. This structure sensitivity is revealed by TOF calculations based on these two types of sites, which correspond to the two main rate controlling steps of the ethanol OSR mechanism, namely steps (ii) and (iii). The materials considered display activity, selectivity, and resistance to aging (manifested by coke deposition and sintering) that are closely related to their initial structure and texture. Two domains in terms of iridium and ceria particle size are identified, leading either to stable and selective catalysts or to unstable and unselective catalysts. Such an original and quantified structure sensitivity analysis should prove useful for further process development. (C) 2011 Published by Elsevier Inc.

[1]  U. Ozkan,et al.  Investigation of the mechanism of ammonia oxidation and oxygen exchange over vanadia catalysts using N-15 and O-18 tracer studies , 1994 .

[2]  Chunshan Song,et al.  Low-temperature reforming of ethanol over CeO2-supported Ni-Rh bimetallic catalysts for hydrogen production , 2005 .

[3]  A. Kiennemann,et al.  Hydrogen production by steam reforming of ethanol Study of mixed oxide catalysts Ce2Zr1.5Me0.5O8 : Comparison of Ni/Co and effect of Rh , 2008 .

[4]  S. Galvagno,et al.  Effect of the acid–base properties of Pd–Ca/Al2O3 catalysts on the selective hydrogenation of phenol to cyclohexanone: FT-IR and TPD characterization , 1998 .

[5]  R. Brink,et al.  The role of the support and dispersion in the catalytic combustion of chlorobenzene on noble metal based catalysts , 2000 .

[6]  Rutger A. van Santen Complementary structure sensitive and insensitive catalytic relationships. , 2009 .

[7]  K. Tomishige,et al.  Catalytic properties and structure of zirconia catalysts for direct synthesis of dimethyl carbonate from methanol and carbon dioxide , 2000 .

[8]  Jean-Claude Lavalley,et al.  Infrared spectrometric studies of the surface basicity of metal oxides and zeolites using adsorbed probe molecules , 1996 .

[9]  F. B. Noronha,et al.  Partial oxidation of ethanol over Pd/CeO2 and Pd/Y2O3 catalysts , 2008 .

[10]  S. Assabumrungrat,et al.  Catalytic steam reforming of ethanol over high surface area CeO2: The role of CeO2 as an internal pre-reforming catalyst , 2006 .

[11]  Manuel Gómez,et al.  Hydrogen production by ethanol reforming over NiZnAl catalysts: Influence of Ce addition on carbon deposition , 2008 .

[12]  Y. Teraoka,et al.  Catalytic decomposition of N2O over CeO2 promoted CO3O4 spinel catalyst , 2007 .

[13]  D. Duprez,et al.  Study of hydrogen surface mobility and hydrogenation reactions over alumina-supported palladium catalysts , 2008 .

[14]  K. Fujimoto,et al.  Reaction Mechanism of Methanol Synthesis from Carbon Dioxide and Hydrogen on Ceria-Supported Palladium Catalysts with SMSI Effect , 1997 .

[15]  P. Ratnasamy,et al.  Influence of the support on the preferential oxidation of CO in hydrogen-rich steam reformates over the CuO–CeO2–ZrO2 system , 2004 .

[16]  J. Kašpar,et al.  A Temperature-Programmed and Transient Kinetic Study of CO2Activation and Methanation over CeO2Supported Noble Metals , 1997 .

[17]  H. Idriss,et al.  H2 Production from Ethanol over Rh–Pt/CeO2 Catalysts: The Role of Rh for the Efficient Dissociation of the Carbon–Carbon Bond , 2002 .

[18]  Masayasu Sato,et al.  Enhanced oxygen storage capacity of cerium oxides in cerium dioxide/lanthanum sesquioxide/alumina containing precious metals , 1990 .

[19]  M. Giona,et al.  A Model for the Temperature-Programmed Reduction of Low and High Surface Area Ceria , 2000 .

[20]  Claude Mirodatos,et al.  Oxidative reforming of biomass derived ethanol for hydrogen production in fuel cell applications , 2002 .

[21]  J. Rasko,et al.  Hydrogen formation in ethanol reforming on supported noble metal catalysts , 2006 .

[22]  D. Duprez,et al.  Oxygen surface mobility and isotopic exchange on oxides: role of the nature and the structure of metal particles , 2000 .

[23]  A. Trovarelli,et al.  Catalytic Properties of Ceria and CeO2-Containing Materials , 1996 .

[24]  Claude Mirodatos,et al.  Ethanol oxidative steam reforming over Ni-based catalysts , 2005 .

[25]  X. Verykios,et al.  Production of hydrogen for fuel cells by reformation of biomass-derived ethanol , 2002 .

[26]  F. B. Noronha,et al.  Hydrogen production for fuel cell applications by ethanol partial oxidation on Pt/CeO2 catalysts: the effect of the reaction conditions and reaction mechanism , 2005 .

[27]  Wenjie Shen,et al.  Hydrogen production by oxidative steam reforming of ethanol over an Ir/CeO2 catalyst , 2007 .

[28]  Xenophon E. Verykios,et al.  Reaction network of steam reforming of ethanol over Ni-based catalysts , 2004 .

[29]  Daniel Duprez,et al.  Bio-ethanol catalytic steam reforming over supported metal catalysts , 2002 .

[30]  Yuhan Sun,et al.  Surface Properties and CO Adsorption on Zirconia Polymorphs , 2005 .

[31]  R. Birringer,et al.  Temperature-Programmed Reaction Spectroscopy of Ceria- and Cu/Ceria-Supported Oxide Catalyst , 2002 .

[32]  D. Duprez,et al.  Oxygen Mobility in CeO2 and CexZr(1-x)O2 Compounds: Study by CO Transient Oxidation and 18O/16O Isotopic Exchange , 1999 .

[33]  Ryōji Takahashi,et al.  BASIC PROPERTIES OF RARE EARTH OXIDES , 2009 .

[34]  D. Duprez,et al.  Ethanol steam reforming over Rh/CexZr1−xO2 catalysts: Impact of the CO–CO2–CH4 interconversion reactions on the H2 production , 2008 .

[35]  G. Bonura,et al.  Steam and auto-thermal reforming of bio-ethanol over MgO and CeO2 Ni supported catalysts , 2006 .

[36]  D. Duprez,et al.  Characterization of the dynamic oxygen migration over Pt/CeO2-ZrO2 catalysts by 18O/16O isotopic exchange reaction , 2004 .

[37]  Qinghong Zhang,et al.  Hydrotalcite-supported gold catalyst for the oxidant-free dehydrogenation of benzyl alcohol: studies on support and gold size effects. , 2011, Chemistry.

[38]  N. Homs,et al.  Use of biofuels to produce hydrogen (reformation processes). , 2008, Chemical Society reviews.

[39]  P. Tsiakaras,et al.  Hydrogen production by ethanol steam reforming over a commercial Pd/γ-Al2O3 catalyst , 2004 .

[40]  M. Engelhard,et al.  Effects of nanocrystalline CeO2 supports on the properties and performance of Ni–Rh bimetallic catalyst for oxidative steam reforming of ethanol , 2006 .

[41]  A. Veen,et al.  Hydrogen production from ethanol over Ir/CeO2 catalysts : A comparative study of steam reforming, partial oxidation and oxidative steam reforming , 2008 .

[42]  T. Egami,et al.  Lattice Defects and Oxygen Storage Capacity of Nanocrystalline Ceria and Ceria-Zirconia , 2000 .

[43]  S. J. Morrison,et al.  A Study of Ethanol Reactions over Pt/CeO2 by Temperature-Programmed Desorption and in Situ FT-IR Spectroscopy: Evidence of Benzene Formation , 2000 .

[44]  Stefano Cavallaro,et al.  Ethanol auto-thermal reforming on rhodium catalysts and initial steps simulation on single crystals under UHV conditions , 2005 .

[45]  Catherine M. Grgicak,et al.  The effect of metal and support particle size on NiO/CeO2 and NiO/ZrO2 catalyst activity in complete methane oxidation , 2007 .

[46]  K. Hidajat,et al.  A crucial role of surface oxygen mobility on nanocrystalline Y2O3 support for oxidative steam reforming of ethanol to hydrogen over Ni/Y2O3 catalysts , 2008 .

[47]  C. Mirodatos,et al.  On-board hydrogen production in a hybrid electric vehicle by bio-ethanol oxidative steam reforming over Ni and noble metal based catalysts , 2003 .

[48]  K. Wilson,et al.  A Fast XPS study of the surface chemistry of ethanol over Pt{1 1 1} , 2004 .

[49]  J. N. Russell,et al.  Bond activation sequence observed in the chemisorption and surface reaction of ethanol on Ni(111) , 1986 .

[50]  S. Goto,et al.  Investigation of isosynthesis via CO hydrogenation over ZrO2 and CeO2 catalysts: Effects of crystallite size, phase composition and acid–base sites , 2007 .

[51]  U. Ozkan,et al.  Ethanol steam reforming over Co-based catalysts: Role of oxygen mobility , 2009 .

[52]  U. Graham,et al.  Steam and CO2 reforming of ethanol over Rh/CeO2 catalyst , 2011 .

[53]  C. Mirodatos Use of isotopic transient kinetics in heterogeneous catalysis , 1991 .

[54]  A. Baiker,et al.  Methane combustion over La0.8Sr0.2MnO3+x supported on MAl2O4 (M = Mg, Ni and Co) spinels , 1994 .

[55]  G. Jacobs,et al.  Steam Reforming of Ethanol over Pt/ceria with Co-fed Hydrogen , 2007 .

[56]  J. Herrmann,et al.  Influence of the reduction/evacuation conditions on the rate of hydrogen spillover on Rh/CeO2 catalysts , 1994 .