The role of the oxidic support on the deactivation of pt catalysts during the CO@2# reforming of methane

J.H. Bitter; J.H. Bitter; W. Hally; W. Hally; Kulathuiyer Seshan; J.G. van Ommen; J.A. Lercher

doi:10.1016/0920-5861(95)00303-7

The role of the oxidic support on the deactivation of pt catalysts during the CO@2# reforming of methane

J.H. Bitter, J.H. Bitter, W. Hally, W. Hally, Kulathuiyer Seshan, J.G. van Ommen, J.A. Lercher

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Abstract

Pt supported on ¿-Al2O3, TiO2 and ZrO2 are active catalysts for the CO2 reforming of methane to synthesis gas. The stability of the catalysts increased in the order Pt/¿-A12O3 < Pt/TiO2 < Pt/ZrO2. For all catalysts, the decrease in activity with time on stream is caused by carbon formation, which blocks the active metal sites for reaction. With Pt/TiO2 and Pt/ZrO2, deactivation started immediately after the start of the reaction, while the Pt/¿-A12O3 catalyst showed an induction period during which carbon was accumulated without affecting the catalytic activity.

Original language	Undefined
Pages (from-to)	349-353
Number of pages	5
Journal	Catalysis today
Volume	29
Issue number	29
DOIs	https://doi.org/10.1016/0920-5861(95)00303-7
Publication status	Published - 1996

Keywords

METIS-105533
IR-10180

Access to Document

10.1016/0920-5861(95)00303-7

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Cite this

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title = "The role of the oxidic support on the deactivation of pt catalysts during the CO@2# reforming of methane",

abstract = "Pt supported on ¿-Al2O3, TiO2 and ZrO2 are active catalysts for the CO2 reforming of methane to synthesis gas. The stability of the catalysts increased in the order Pt/¿-A12O3 < Pt/TiO2 < Pt/ZrO2. For all catalysts, the decrease in activity with time on stream is caused by carbon formation, which blocks the active metal sites for reaction. With Pt/TiO2 and Pt/ZrO2, deactivation started immediately after the start of the reaction, while the Pt/¿-A12O3 catalyst showed an induction period during which carbon was accumulated without affecting the catalytic activity.",

keywords = "METIS-105533, IR-10180",

author = "J.H. Bitter and J.H. Bitter and W. Hally and W. Hally and Kulathuiyer Seshan and {van Ommen}, J.G. and J.A. Lercher",

year = "1996",

doi = "10.1016/0920-5861(95)00303-7",

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volume = "29",

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journal = "Catalysis today",

issn = "0920-5861",

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T1 - The role of the oxidic support on the deactivation of pt catalysts during the CO@2# reforming of methane

AU - Bitter, J.H.

AU - Hally, W.

AU - Seshan, Kulathuiyer

AU - van Ommen, J.G.

AU - Lercher, J.A.

PY - 1996

Y1 - 1996

N2 - Pt supported on ¿-Al2O3, TiO2 and ZrO2 are active catalysts for the CO2 reforming of methane to synthesis gas. The stability of the catalysts increased in the order Pt/¿-A12O3 < Pt/TiO2 < Pt/ZrO2. For all catalysts, the decrease in activity with time on stream is caused by carbon formation, which blocks the active metal sites for reaction. With Pt/TiO2 and Pt/ZrO2, deactivation started immediately after the start of the reaction, while the Pt/¿-A12O3 catalyst showed an induction period during which carbon was accumulated without affecting the catalytic activity.

AB - Pt supported on ¿-Al2O3, TiO2 and ZrO2 are active catalysts for the CO2 reforming of methane to synthesis gas. The stability of the catalysts increased in the order Pt/¿-A12O3 < Pt/TiO2 < Pt/ZrO2. For all catalysts, the decrease in activity with time on stream is caused by carbon formation, which blocks the active metal sites for reaction. With Pt/TiO2 and Pt/ZrO2, deactivation started immediately after the start of the reaction, while the Pt/¿-A12O3 catalyst showed an induction period during which carbon was accumulated without affecting the catalytic activity.

KW - METIS-105533

KW - IR-10180

U2 - 10.1016/0920-5861(95)00303-7

DO - 10.1016/0920-5861(95)00303-7

M3 - Article

VL - 29

SP - 349

EP - 353

JO - Catalysis today

JF - Catalysis today

SN - 0920-5861

IS - 29

ER -