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In Situ XPS and MS Study of Methane Oxidation on the Pd–Pt/Al2O3 Catalysts. / Chetyrin, Igor A.; Bukhtiyarov, Andrey V.; Prosvirin, Igor P. et al.

In: Topics in Catalysis, Vol. 63, No. 1-2, 01.03.2020, p. 66-74.

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Harvard

Chetyrin, IA, Bukhtiyarov, AV, Prosvirin, IP, Khudorozhkov, AK & Bukhtiyarov, VI 2020, 'In Situ XPS and MS Study of Methane Oxidation on the Pd–Pt/Al2O3 Catalysts', Topics in Catalysis, vol. 63, no. 1-2, pp. 66-74. https://doi.org/10.1007/s11244-019-01217-7

APA

Vancouver

Chetyrin IA, Bukhtiyarov AV, Prosvirin IP, Khudorozhkov AK, Bukhtiyarov VI. In Situ XPS and MS Study of Methane Oxidation on the Pd–Pt/Al2O3 Catalysts. Topics in Catalysis. 2020 Mar 1;63(1-2):66-74. doi: 10.1007/s11244-019-01217-7

Author

Chetyrin, Igor A. ; Bukhtiyarov, Andrey V. ; Prosvirin, Igor P. et al. / In Situ XPS and MS Study of Methane Oxidation on the Pd–Pt/Al2O3 Catalysts. In: Topics in Catalysis. 2020 ; Vol. 63, No. 1-2. pp. 66-74.

BibTeX

@article{3b5b20faf13d4ae18153ecbc54a5a066,
title = "In Situ XPS and MS Study of Methane Oxidation on the Pd–Pt/Al2O3 Catalysts",
abstract = "The bimetallic Pd–Pt/Al2O3 supported catalysts with different Pd/Pt ratios have been prepared and studied in methane oxidation reaction. Comparison of their catalytic properties with those of monometallic Pd/Al2O3 and Pt/Al2O3 samples has shown that the bimetallic catalysts with a relatively low Pt loading (less than 0.4 mol%) are more active than the monometallic ones indicating the synergy effect. An increase in Pt loading above 0.5 mol% decreases the catalytic activity, so that these catalysts become less active than the monometallic Pd/Al2O3 catalysts, but still keep an activity higher than that of the least active monometallic Pt/Al2O3 sample. The chemical states of the palladium and platinum for all the catalysts produced depending on the reaction conditions have been investigated with in situ XPS. It has been shown that even at room temperature the reaction mixture affects the surface composition of the catalysts, which does not change much at higher reaction temperatures. The data have led us to suggestion that activity in the total methane oxidation is promoted by formation of Pd2+, surface fraction of which depends on Pt content in the bimetallic catalysts.",
keywords = "Bimetallic Pd–Pt catalysts, In situ measurements, Methane oxidation, X-ray photoelectron spectroscopy, SIZE, COPPER, ALUMINA, PRESSURE, PD, COMBUSTION ACTIVITY, Bimetallic Pd-Pt catalysts, RAY PHOTOELECTRON-SPECTROSCOPY, PD(111) OXIDATION, METAL, BIMETALLIC CATALYSTS",
author = "Chetyrin, {Igor A.} and Bukhtiyarov, {Andrey V.} and Prosvirin, {Igor P.} and Khudorozhkov, {Alexander K.} and Bukhtiyarov, {Valerii I.}",
year = "2020",
month = mar,
day = "1",
doi = "10.1007/s11244-019-01217-7",
language = "English",
volume = "63",
pages = "66--74",
journal = "Topics in Catalysis",
issn = "1022-5528",
publisher = "Springer Netherlands",
number = "1-2",

}

RIS

TY - JOUR

T1 - In Situ XPS and MS Study of Methane Oxidation on the Pd–Pt/Al2O3 Catalysts

AU - Chetyrin, Igor A.

AU - Bukhtiyarov, Andrey V.

AU - Prosvirin, Igor P.

AU - Khudorozhkov, Alexander K.

AU - Bukhtiyarov, Valerii I.

PY - 2020/3/1

Y1 - 2020/3/1

N2 - The bimetallic Pd–Pt/Al2O3 supported catalysts with different Pd/Pt ratios have been prepared and studied in methane oxidation reaction. Comparison of their catalytic properties with those of monometallic Pd/Al2O3 and Pt/Al2O3 samples has shown that the bimetallic catalysts with a relatively low Pt loading (less than 0.4 mol%) are more active than the monometallic ones indicating the synergy effect. An increase in Pt loading above 0.5 mol% decreases the catalytic activity, so that these catalysts become less active than the monometallic Pd/Al2O3 catalysts, but still keep an activity higher than that of the least active monometallic Pt/Al2O3 sample. The chemical states of the palladium and platinum for all the catalysts produced depending on the reaction conditions have been investigated with in situ XPS. It has been shown that even at room temperature the reaction mixture affects the surface composition of the catalysts, which does not change much at higher reaction temperatures. The data have led us to suggestion that activity in the total methane oxidation is promoted by formation of Pd2+, surface fraction of which depends on Pt content in the bimetallic catalysts.

AB - The bimetallic Pd–Pt/Al2O3 supported catalysts with different Pd/Pt ratios have been prepared and studied in methane oxidation reaction. Comparison of their catalytic properties with those of monometallic Pd/Al2O3 and Pt/Al2O3 samples has shown that the bimetallic catalysts with a relatively low Pt loading (less than 0.4 mol%) are more active than the monometallic ones indicating the synergy effect. An increase in Pt loading above 0.5 mol% decreases the catalytic activity, so that these catalysts become less active than the monometallic Pd/Al2O3 catalysts, but still keep an activity higher than that of the least active monometallic Pt/Al2O3 sample. The chemical states of the palladium and platinum for all the catalysts produced depending on the reaction conditions have been investigated with in situ XPS. It has been shown that even at room temperature the reaction mixture affects the surface composition of the catalysts, which does not change much at higher reaction temperatures. The data have led us to suggestion that activity in the total methane oxidation is promoted by formation of Pd2+, surface fraction of which depends on Pt content in the bimetallic catalysts.

KW - Bimetallic Pd–Pt catalysts

KW - In situ measurements

KW - Methane oxidation

KW - X-ray photoelectron spectroscopy

KW - SIZE

KW - COPPER

KW - ALUMINA

KW - PRESSURE

KW - PD

KW - COMBUSTION ACTIVITY

KW - Bimetallic Pd-Pt catalysts

KW - RAY PHOTOELECTRON-SPECTROSCOPY

KW - PD(111) OXIDATION

KW - METAL

KW - BIMETALLIC CATALYSTS

UR - http://www.scopus.com/inward/record.url?scp=85077588863&partnerID=8YFLogxK

U2 - 10.1007/s11244-019-01217-7

DO - 10.1007/s11244-019-01217-7

M3 - Article

AN - SCOPUS:85077588863

VL - 63

SP - 66

EP - 74

JO - Topics in Catalysis

JF - Topics in Catalysis

SN - 1022-5528

IS - 1-2

ER -

ID: 23120947