In this work, catalysts based on palladium supported on alumina and zirconia were prepared by wet impregnation method and calcined at 600 degrees C and 1000 degrees C. All the samples were characterized by surface area measurements (BET), X-ray diffraction (XRD), X-ray photoelectronic spectroscopy (XPS), and temperature desorption of oxygen (O-2-TPD), and were tested in the combustion of methane using temperature-programmed surface reaction (TPSR). The results indicated that alumina supported catalysts calcined at 600 degrees C were slightly more active than zirconia supported catalysts, but after heat treatment at 1000 degrees C, palladium catalyst supported on zirconia presented better performance above 500 degrees C. The O-2-TPD pattern of temperature between the range of stability of PdOx species and activity was observed, where a better PdOx stability was associated with more active catalysts. The aim of this study is to understand the behavior of the Pd catalysts in the combustion of methane by analyzing the effect of the support (alumina or zirconia) and of the heat treatment (600 degrees C or 1000 degrees C) using a simple experimental approach.
机构:
Max Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, GermanyMax Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, Germany
Schauermann, S
Johánek, V
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Max Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, GermanyMax Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, Germany
Johánek, V
Laurin, M
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Max Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, GermanyMax Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, Germany
Laurin, M
Libuda, J
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Max Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, GermanyMax Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, Germany
Libuda, J
Freund, HJ
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Max Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, GermanyMax Planck Gesell, Fritz Haber Inst, Dept Chem Phys, D-14195 Berlin, Germany
机构:
UNIV CLAUDE BERNARD LYON 1,INST RECH CATALYSE,PROPRE CONVENT LAB,2 AVE ALBERT EINSTEIN,F-69626 VILLEURBANNE,FRANCEUNIV CLAUDE BERNARD LYON 1,INST RECH CATALYSE,PROPRE CONVENT LAB,2 AVE ALBERT EINSTEIN,F-69626 VILLEURBANNE,FRANCE
HOYOS, LJ
PRALIAUD, H
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UNIV CLAUDE BERNARD LYON 1,INST RECH CATALYSE,PROPRE CONVENT LAB,2 AVE ALBERT EINSTEIN,F-69626 VILLEURBANNE,FRANCEUNIV CLAUDE BERNARD LYON 1,INST RECH CATALYSE,PROPRE CONVENT LAB,2 AVE ALBERT EINSTEIN,F-69626 VILLEURBANNE,FRANCE
PRALIAUD, H
PRIMET, M
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UNIV CLAUDE BERNARD LYON 1,INST RECH CATALYSE,PROPRE CONVENT LAB,2 AVE ALBERT EINSTEIN,F-69626 VILLEURBANNE,FRANCEUNIV CLAUDE BERNARD LYON 1,INST RECH CATALYSE,PROPRE CONVENT LAB,2 AVE ALBERT EINSTEIN,F-69626 VILLEURBANNE,FRANCE
机构:
School of Resource and Safety Engineering,China University of Mining and Technology(Beijing)
China Coal Information InstituteSchool of Resource and Safety Engineering,China University of Mining and Technology(Beijing)
Liu Wenge
Guo Deyong
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School of Resource and Safety Engineering,China University of Mining and Technology(Beijing)School of Resource and Safety Engineering,China University of Mining and Technology(Beijing)
Guo Deyong
Xu Xin
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China Coal Information InstituteSchool of Resource and Safety Engineering,China University of Mining and Technology(Beijing)
机构:
China Univ Min & Technol Beijing, Sch Resource & Safety Engn, Beijing 100083, Peoples R China
China Coal Informat Inst, Beijing 100029, Peoples R ChinaChina Univ Min & Technol Beijing, Sch Resource & Safety Engn, Beijing 100083, Peoples R China
Liu Wenge
Guo Deyong
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机构:
China Univ Min & Technol Beijing, Sch Resource & Safety Engn, Beijing 100083, Peoples R ChinaChina Univ Min & Technol Beijing, Sch Resource & Safety Engn, Beijing 100083, Peoples R China
Guo Deyong
Xu Xin
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China Coal Informat Inst, Beijing 100029, Peoples R ChinaChina Univ Min & Technol Beijing, Sch Resource & Safety Engn, Beijing 100083, Peoples R China