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Effect of Pt addition on sulfur dioxide and water vapor tolerance of Pd-Mn-hexaaluminate catalysts for high-temperature oxidation of methane. / Yashnik, S. A.; Chesalov, Yu A.; Ishchenko, A. V. et al.

In: Applied Catalysis B: Environmental, Vol. 204, 05.05.2017, p. 89-106.

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Yashnik SA, Chesalov YA, Ishchenko AV, Kaichev VV, Ismagilov ZR. Effect of Pt addition on sulfur dioxide and water vapor tolerance of Pd-Mn-hexaaluminate catalysts for high-temperature oxidation of methane. Applied Catalysis B: Environmental. 2017 May 5;204:89-106. doi: 10.1016/j.apcatb.2016.11.018

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Yashnik, S. A. ; Chesalov, Yu A. ; Ishchenko, A. V. et al. / Effect of Pt addition on sulfur dioxide and water vapor tolerance of Pd-Mn-hexaaluminate catalysts for high-temperature oxidation of methane. In: Applied Catalysis B: Environmental. 2017 ; Vol. 204. pp. 89-106.

BibTeX

@article{842fce969aa44ef78915b5a84a20bada,
title = "Effect of Pt addition on sulfur dioxide and water vapor tolerance of Pd-Mn-hexaaluminate catalysts for high-temperature oxidation of methane",
abstract = "An effect of Pt addition to improve the catalytic performance of Pd-modified Mn-hexaaluminate in the high-temperature oxidation of methane, especially in SO2 and water presence, has been studied. X-ray diffraction, high-resolution transmission electron microscopy, X-ray photoelectron spectroscopy, thermogravimetry and differential thermal analysis were used for the characterization of fresh and spent catalysts. Temperature-programmed reduction by hydrogen was employed to study the redox properties of the catalysts. Four high-temperature tests (at 670 °C) of the methane oxidation were applied to reveal the water and sulfur resistance of the catalysts: 1) dry methane-air feed; 2) wet methane-air feed containing 3 wt% of water vapor; 3) methane-air feed containing 1000 ppm of SO2; and 4) wet methane-air feed with 1000 ppm of SO2. The Pt-doped Pd-Mn-hexaaluminate catalyst with the atomic ratio of Pt/Pd < 0.3 has been shown to possess the highest catalytic activity in the oxidation of methane, high water and sulfur tolerance, and reducibility by hydrogen as compared to the monometallic Pd-Mn-hexaaluminate catalyst and the bimetallic catalysts with Pt/Pd > 0.5. From the formal kinetic data of the oxidation of methane on the fresh and deactivated catalysts, we assumed that deactivation of the catalysts is due to a decrease in the amount of catalytically active sites in the bimetallic 0.33Pt-0.67Pd(0.27)/MnLaAl11O19 catalyst and a change in the state of active component in the other catalysts. Their oxidation ability and redox behavior were shown to be associated with the highly dispersed PdO particles, a PdO layer (3–5 nm) covering the metal palladium particles as well as the Mn3+-enriched MnLaAl11O19. The improved water and sulfur resistance is found to correlate with the presence of particles of PtPd alloy, with its fraction not exceeding 50%.",
keywords = "Methane oxidation, Mn-hexaaluminate, Pd-catalyst, Pt-catalyst, Sulfur-resistance, NOBLE-METAL CATALYSTS, SUPPORTED PALLADIUM CATALYSTS, HYDROGEN-SULFIDE, GAMMA-ALUMINA, COMBUSTION CATALYSTS, PT/AL2O3 CATALYSTS, GAS ENGINE EXHAUST, PDO/AL2O3 CATALYST, PROPANE OXIDATION, PT CATALYSTS",
author = "Yashnik, {S. A.} and Chesalov, {Yu A.} and Ishchenko, {A. V.} and Kaichev, {V. V.} and Ismagilov, {Z. R.}",
year = "2017",
month = may,
day = "5",
doi = "10.1016/j.apcatb.2016.11.018",
language = "English",
volume = "204",
pages = "89--106",
journal = "Applied Catalysis B: Environmental",
issn = "0926-3373",
publisher = "Elsevier",

}

RIS

TY - JOUR

T1 - Effect of Pt addition on sulfur dioxide and water vapor tolerance of Pd-Mn-hexaaluminate catalysts for high-temperature oxidation of methane

AU - Yashnik, S. A.

AU - Chesalov, Yu A.

AU - Ishchenko, A. V.

AU - Kaichev, V. V.

AU - Ismagilov, Z. R.

PY - 2017/5/5

Y1 - 2017/5/5

N2 - An effect of Pt addition to improve the catalytic performance of Pd-modified Mn-hexaaluminate in the high-temperature oxidation of methane, especially in SO2 and water presence, has been studied. X-ray diffraction, high-resolution transmission electron microscopy, X-ray photoelectron spectroscopy, thermogravimetry and differential thermal analysis were used for the characterization of fresh and spent catalysts. Temperature-programmed reduction by hydrogen was employed to study the redox properties of the catalysts. Four high-temperature tests (at 670 °C) of the methane oxidation were applied to reveal the water and sulfur resistance of the catalysts: 1) dry methane-air feed; 2) wet methane-air feed containing 3 wt% of water vapor; 3) methane-air feed containing 1000 ppm of SO2; and 4) wet methane-air feed with 1000 ppm of SO2. The Pt-doped Pd-Mn-hexaaluminate catalyst with the atomic ratio of Pt/Pd < 0.3 has been shown to possess the highest catalytic activity in the oxidation of methane, high water and sulfur tolerance, and reducibility by hydrogen as compared to the monometallic Pd-Mn-hexaaluminate catalyst and the bimetallic catalysts with Pt/Pd > 0.5. From the formal kinetic data of the oxidation of methane on the fresh and deactivated catalysts, we assumed that deactivation of the catalysts is due to a decrease in the amount of catalytically active sites in the bimetallic 0.33Pt-0.67Pd(0.27)/MnLaAl11O19 catalyst and a change in the state of active component in the other catalysts. Their oxidation ability and redox behavior were shown to be associated with the highly dispersed PdO particles, a PdO layer (3–5 nm) covering the metal palladium particles as well as the Mn3+-enriched MnLaAl11O19. The improved water and sulfur resistance is found to correlate with the presence of particles of PtPd alloy, with its fraction not exceeding 50%.

AB - An effect of Pt addition to improve the catalytic performance of Pd-modified Mn-hexaaluminate in the high-temperature oxidation of methane, especially in SO2 and water presence, has been studied. X-ray diffraction, high-resolution transmission electron microscopy, X-ray photoelectron spectroscopy, thermogravimetry and differential thermal analysis were used for the characterization of fresh and spent catalysts. Temperature-programmed reduction by hydrogen was employed to study the redox properties of the catalysts. Four high-temperature tests (at 670 °C) of the methane oxidation were applied to reveal the water and sulfur resistance of the catalysts: 1) dry methane-air feed; 2) wet methane-air feed containing 3 wt% of water vapor; 3) methane-air feed containing 1000 ppm of SO2; and 4) wet methane-air feed with 1000 ppm of SO2. The Pt-doped Pd-Mn-hexaaluminate catalyst with the atomic ratio of Pt/Pd < 0.3 has been shown to possess the highest catalytic activity in the oxidation of methane, high water and sulfur tolerance, and reducibility by hydrogen as compared to the monometallic Pd-Mn-hexaaluminate catalyst and the bimetallic catalysts with Pt/Pd > 0.5. From the formal kinetic data of the oxidation of methane on the fresh and deactivated catalysts, we assumed that deactivation of the catalysts is due to a decrease in the amount of catalytically active sites in the bimetallic 0.33Pt-0.67Pd(0.27)/MnLaAl11O19 catalyst and a change in the state of active component in the other catalysts. Their oxidation ability and redox behavior were shown to be associated with the highly dispersed PdO particles, a PdO layer (3–5 nm) covering the metal palladium particles as well as the Mn3+-enriched MnLaAl11O19. The improved water and sulfur resistance is found to correlate with the presence of particles of PtPd alloy, with its fraction not exceeding 50%.

KW - Methane oxidation

KW - Mn-hexaaluminate

KW - Pd-catalyst

KW - Pt-catalyst

KW - Sulfur-resistance

KW - NOBLE-METAL CATALYSTS

KW - SUPPORTED PALLADIUM CATALYSTS

KW - HYDROGEN-SULFIDE

KW - GAMMA-ALUMINA

KW - COMBUSTION CATALYSTS

KW - PT/AL2O3 CATALYSTS

KW - GAS ENGINE EXHAUST

KW - PDO/AL2O3 CATALYST

KW - PROPANE OXIDATION

KW - PT CATALYSTS

UR - http://www.scopus.com/inward/record.url?scp=84997235763&partnerID=8YFLogxK

U2 - 10.1016/j.apcatb.2016.11.018

DO - 10.1016/j.apcatb.2016.11.018

M3 - Article

AN - SCOPUS:84997235763

VL - 204

SP - 89

EP - 106

JO - Applied Catalysis B: Environmental

JF - Applied Catalysis B: Environmental

SN - 0926-3373

ER -

ID: 10318395