2016
DOI: 10.1016/j.molcata.2015.08.001
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Low-temperature oxidation of methane on Pd-Sn/ZrO2 catalysts

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Cited by 17 publications
(6 citation statements)
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“…According to several previous studies, the negative peak below 100 °C was corresponded to the H 2 desorption as a result of the decomposition of Pd hydride, [36] such as α-H-Pd, β-H-Pd and γ-H-Pd. [33,37] In addition, the broad and small peak located between 100 °C and 200 °C can be assigned to the reduction of strong absorbed PdO species. [38] Typically, when hydrogen is passed over the Pd supported catalysts at room temperature, hydrogen is consumed rapidly.…”
Section: Tem Observationsmentioning
confidence: 99%
“…According to several previous studies, the negative peak below 100 °C was corresponded to the H 2 desorption as a result of the decomposition of Pd hydride, [36] such as α-H-Pd, β-H-Pd and γ-H-Pd. [33,37] In addition, the broad and small peak located between 100 °C and 200 °C can be assigned to the reduction of strong absorbed PdO species. [38] Typically, when hydrogen is passed over the Pd supported catalysts at room temperature, hydrogen is consumed rapidly.…”
Section: Tem Observationsmentioning
confidence: 99%
“…[6][7][8][9] So far, the simple metal oxides, such as CeO 2 , Co 3 O 4 , TiO 2 , ZrO 2 and MnO x , have been extensively studied for their large specic surface area. [10][11][12][13] Whereas in practical applications, metal oxide supported catalysts are unstable aer redox cycling, which results in the deactivation of active Pd species.…”
Section: Introductionmentioning
confidence: 99%
“…The performance of Pd‐based catalysts depend not only on the supported active species, but also on the nature of the supports. For example, Pd/ZrO 2 catalyst had high thermal stability, but they showed poor activity due to its irreducibility [11] . SiO 2 ‐supported Pd catalysts had large specific surface area, whereas they exhibited poor hydrothermal stability [12] .…”
Section: Introductionmentioning
confidence: 99%