2000
DOI: 10.1006/jcat.2000.2967
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Palladium, Palladium–Tin, and Palladium–Silver Catalysts in the Selective Hydrogenation of Hexadienes: TPR, Mössbauer, and Infrared Studies of Adsorbed CO

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Cited by 66 publications
(32 citation statements)
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“…To investigate the oxidation states and the accessibility of the exposed metals in the Pd-Sn catalysts, CO adsorption was followed by IR spectroscopy. For Sn_Al one band is observed at 2199 cm )1 (not shown), which can be ascribed either to adsorption of CO on Sn 4+ [34] or to CO interacting with A1 3+ on the alumina surface [35]. The band disappeared after evacuation of the cell at 25°C.…”
Section: Catalyst Characterizationmentioning
confidence: 94%
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“…To investigate the oxidation states and the accessibility of the exposed metals in the Pd-Sn catalysts, CO adsorption was followed by IR spectroscopy. For Sn_Al one band is observed at 2199 cm )1 (not shown), which can be ascribed either to adsorption of CO on Sn 4+ [34] or to CO interacting with A1 3+ on the alumina surface [35]. The band disappeared after evacuation of the cell at 25°C.…”
Section: Catalyst Characterizationmentioning
confidence: 94%
“…After evacuation at 298 K, the band at around 1988 cm )1 decreased in intensity and shifted to lower wave numbers, whereas the carbonyl species giving the band near 1930 cm )1 were unaffected. Sales et al [35] observed only one very broad band centred at 1980 cm )1 for Pd- Sn supported on alumina catalysts, a feature which they attributed this feature to three different types of bridged CO species adsorbed on metallic palladium. The band near 1930 cm )1 in the spectra ( figure 4 a, b) are ascribed to compressed bridged CO species adsorbed on high index planes of metallic Pd or to CO in threefold sites on Pd [35].…”
Section: Catalyst Characterizationmentioning
confidence: 96%
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“…Other authors suggest that the consumption of hydrogen near these temperatures is due to the reduction of Pd η+ Cl x O y (0 < η < 2) species or to the reduction of Pd +2 ions stabilized by neighbouring Cl -, that were not eliminated during calcination and remain on the alumina surface. [26][27][28] Figure 3 shows that above 503 K multiple hydrogen consumption peaks appear due to the reduction of NiO species that interact with the support. The first peaks at 520-620 can be assigned to the reduction of NiO x with weak or null interaction with the support (bulk NiO).…”
Section: Catalysts Characterizationmentioning
confidence: 99%