Steam-methane reforming at low temperature on nickel-based catalysts

[Display omitted] •A Ni–Zn–Al catalyst is active and stable for steam-methane reforming at low temperatures.•Ni–Zn–Al catalyst is resistant to sintering and inhibits formation of carbonaceous deposits.•Ni–Mg–Al catalyst is active for steam-methane reforming but produces carbon nanofibers.•Intimate c...

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Veröffentlicht in:Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2014-01, Vol.235, p.158-166
Hauptverfasser: Nieva, María A., Villaverde, María M., Monzón, Antonio, Garetto, Teresita F., Marchi, Alberto J.
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container_title Chemical engineering journal (Lausanne, Switzerland : 1996)
container_volume 235
creator Nieva, María A.
Villaverde, María M.
Monzón, Antonio
Garetto, Teresita F.
Marchi, Alberto J.
description [Display omitted] •A Ni–Zn–Al catalyst is active and stable for steam-methane reforming at low temperatures.•Ni–Zn–Al catalyst is resistant to sintering and inhibits formation of carbonaceous deposits.•Ni–Mg–Al catalyst is active for steam-methane reforming but produces carbon nanofibers.•Intimate contact between Ni and spinel-like matrix is crucial for metal phase activity and stability. In this work, we report the activity results obtained in steam-methane reforming (SMR) at 500 and 600°C using four nickel-based catalysts: (a) Ni/α-Al2O3 and Ni/SiO2, prepared by incipient wetness impregnation method and (b) Ni–Zn–Al and Ni–Mg–Al, prepared by coprecipitation method. In all of the samples, the nickel load ranged between 7% and 9%. The catalytic activity in SMR at steady state followed the pattern: Ni–Mg–Al≅Ni–Zn–Al>Ni/α-Al2O3>Ni/SiO2. According to characterization results, the interaction between Ni2+ species and support in precursor oxides was stronger in Ni–Mg–Al and Ni–Zn–Al than in Ni/α-Al2O3 and Ni/SiO2. After activation in H2 flow, large metal nickel particles with low or none interaction with the support were obtained in the case of Ni/α-Al2O3 and Ni/SiO2. On the contrary, small metal particles, between 3 and 6nm, in high interaction with support were obtained in Ni–Zn–Al and Ni–Mg–Al catalysts. The metal phase formed in Ni–Mg–Al and Ni–Zn–Al was the most active and resistant to sintering under reaction conditions at T⩽600°C. It was also found that carbon nanofibers were formed on Ni/α-Al2O3, Ni/SiO2 and Ni–Mg–Al catalysts during SMR at 600°C. The amount and diameter of nanofibers formed on Ni–Mg–Al were lower than on catalysts prepared by impregnation method, which is in agreement with the relative sizes of metal nickel particles in each case. Amazingly, no filamentary carbon was detected on the used Ni–Zn–Al sample: only amorphous coke in low amounts was formed. This was attributed to the proper interaction of small metal nickel particles with the non-stoichiometric zinc aluminate-like phase formed after thermal treatments of catalyst precursor.
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In this work, we report the activity results obtained in steam-methane reforming (SMR) at 500 and 600°C using four nickel-based catalysts: (a) Ni/α-Al2O3 and Ni/SiO2, prepared by incipient wetness impregnation method and (b) Ni–Zn–Al and Ni–Mg–Al, prepared by coprecipitation method. In all of the samples, the nickel load ranged between 7% and 9%. The catalytic activity in SMR at steady state followed the pattern: Ni–Mg–Al≅Ni–Zn–Al&gt;Ni/α-Al2O3&gt;Ni/SiO2. According to characterization results, the interaction between Ni2+ species and support in precursor oxides was stronger in Ni–Mg–Al and Ni–Zn–Al than in Ni/α-Al2O3 and Ni/SiO2. After activation in H2 flow, large metal nickel particles with low or none interaction with the support were obtained in the case of Ni/α-Al2O3 and Ni/SiO2. On the contrary, small metal particles, between 3 and 6nm, in high interaction with support were obtained in Ni–Zn–Al and Ni–Mg–Al catalysts. The metal phase formed in Ni–Mg–Al and Ni–Zn–Al was the most active and resistant to sintering under reaction conditions at T⩽600°C. It was also found that carbon nanofibers were formed on Ni/α-Al2O3, Ni/SiO2 and Ni–Mg–Al catalysts during SMR at 600°C. The amount and diameter of nanofibers formed on Ni–Mg–Al were lower than on catalysts prepared by impregnation method, which is in agreement with the relative sizes of metal nickel particles in each case. Amazingly, no filamentary carbon was detected on the used Ni–Zn–Al sample: only amorphous coke in low amounts was formed. 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In this work, we report the activity results obtained in steam-methane reforming (SMR) at 500 and 600°C using four nickel-based catalysts: (a) Ni/α-Al2O3 and Ni/SiO2, prepared by incipient wetness impregnation method and (b) Ni–Zn–Al and Ni–Mg–Al, prepared by coprecipitation method. In all of the samples, the nickel load ranged between 7% and 9%. The catalytic activity in SMR at steady state followed the pattern: Ni–Mg–Al≅Ni–Zn–Al&gt;Ni/α-Al2O3&gt;Ni/SiO2. According to characterization results, the interaction between Ni2+ species and support in precursor oxides was stronger in Ni–Mg–Al and Ni–Zn–Al than in Ni/α-Al2O3 and Ni/SiO2. After activation in H2 flow, large metal nickel particles with low or none interaction with the support were obtained in the case of Ni/α-Al2O3 and Ni/SiO2. On the contrary, small metal particles, between 3 and 6nm, in high interaction with support were obtained in Ni–Zn–Al and Ni–Mg–Al catalysts. The metal phase formed in Ni–Mg–Al and Ni–Zn–Al was the most active and resistant to sintering under reaction conditions at T⩽600°C. It was also found that carbon nanofibers were formed on Ni/α-Al2O3, Ni/SiO2 and Ni–Mg–Al catalysts during SMR at 600°C. The amount and diameter of nanofibers formed on Ni–Mg–Al were lower than on catalysts prepared by impregnation method, which is in agreement with the relative sizes of metal nickel particles in each case. Amazingly, no filamentary carbon was detected on the used Ni–Zn–Al sample: only amorphous coke in low amounts was formed. 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In this work, we report the activity results obtained in steam-methane reforming (SMR) at 500 and 600°C using four nickel-based catalysts: (a) Ni/α-Al2O3 and Ni/SiO2, prepared by incipient wetness impregnation method and (b) Ni–Zn–Al and Ni–Mg–Al, prepared by coprecipitation method. In all of the samples, the nickel load ranged between 7% and 9%. The catalytic activity in SMR at steady state followed the pattern: Ni–Mg–Al≅Ni–Zn–Al&gt;Ni/α-Al2O3&gt;Ni/SiO2. According to characterization results, the interaction between Ni2+ species and support in precursor oxides was stronger in Ni–Mg–Al and Ni–Zn–Al than in Ni/α-Al2O3 and Ni/SiO2. After activation in H2 flow, large metal nickel particles with low or none interaction with the support were obtained in the case of Ni/α-Al2O3 and Ni/SiO2. On the contrary, small metal particles, between 3 and 6nm, in high interaction with support were obtained in Ni–Zn–Al and Ni–Mg–Al catalysts. The metal phase formed in Ni–Mg–Al and Ni–Zn–Al was the most active and resistant to sintering under reaction conditions at T⩽600°C. It was also found that carbon nanofibers were formed on Ni/α-Al2O3, Ni/SiO2 and Ni–Mg–Al catalysts during SMR at 600°C. The amount and diameter of nanofibers formed on Ni–Mg–Al were lower than on catalysts prepared by impregnation method, which is in agreement with the relative sizes of metal nickel particles in each case. Amazingly, no filamentary carbon was detected on the used Ni–Zn–Al sample: only amorphous coke in low amounts was formed. This was attributed to the proper interaction of small metal nickel particles with the non-stoichiometric zinc aluminate-like phase formed after thermal treatments of catalyst precursor.</abstract><pub>Elsevier B.V</pub><doi>10.1016/j.cej.2013.09.030</doi><tpages>9</tpages><oa>free_for_read</oa></addata></record>
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1873-3212
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source Elsevier ScienceDirect Journals
subjects Catalysis
Catalysts
Hydrogen
Impregnation
Metal–support interaction
Nickel
Nickel catalysts
Precursors
Reforming
Silicon dioxide
Steam-methane reforming
Synthesis gas
Zinc
title Steam-methane reforming at low temperature on nickel-based catalysts
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