PtNi catalysts prepared via borohydride reduction for hydrogenation of benzene

Pt/Ni–silica catalysts were prepared via co and step impregnation using NaBH 4 as a reducing agent. Pt 55Ni 45-CI (co-impregnated) exhibited superior reactivity compared to the monometallic catalysts. Alloying and Pt segregation may contribute to this enhanced activity. Pt/Ni supported on silica cat...

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Published inJournal of catalysis Vol. 265; no. 1; pp. 63 - 71
Main Authors Abu Bakar, N.H.H., Bettahar, M.M., Abu Bakar, M., Monteverdi, S., Ismail, J., Alnot, M.
Format Journal Article
LanguageEnglish
Published Amsterdam Elsevier Inc 01.07.2009
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Abstract Pt/Ni–silica catalysts were prepared via co and step impregnation using NaBH 4 as a reducing agent. Pt 55Ni 45-CI (co-impregnated) exhibited superior reactivity compared to the monometallic catalysts. Alloying and Pt segregation may contribute to this enhanced activity. Pt/Ni supported on silica catalysts were synthesized via co-impregnation (CI) and step-impregnation (SI) techniques using NaBH 4 as the metal ions reducing agent. They were characterized by H 2-TPR and H 2-TPD, XRD, TEM, SEM and EDSX analyses as well as tested for the hydrogenation of benzene. The preparation method employed facilitates the formation of totally reduced pure metal or bimetallic metal particles on the surface and catalytic properties are governed by both the Pt/Ni ratio and mode of preparation. Co-impregnated catalysts exhibit a synergistic effect when a moderate amount of Pt is available: Pt 55Ni 45-CI catalyst was more active than both the pure monometallic catalysts. XRD and SEM equipped with EDSX lead us to believe that alloying occurs in the catalyst. Furthermore, surface segregation of Pt on the alloys as proven by XPS also contributes to this enhanced reactivity. In contrast to co-impregnated catalyst, all the step-impregnated catalysts show low catalytic reactivity when compared to pure Pt.
AbstractList Pt/Ni-silica catalysts were prepared via co and step impregnation using NaBH4 as a reducing agent. Pt55 Ni45 -CI (co-impregnated) exhibited superior reactivity compared to the monometallic catalysts. Alloying and Pt segregation may contribute to this enhanced activity. Pt/Ni supported on silica catalysts were synthesized via co-impregnation (CI) and step-impregnation (SI) techniques using NaBH4 as the metal ions reducing agent. They were characterized by H2 -TPR and H2 -TPD, XRD, TEM, SEM and EDSX analyses as well as tested for the hydrogenation of benzene. The preparation method employed facilitates the formation of totally reduced pure metal or bimetallic metal particles on the surface and catalytic properties are governed by both the Pt/Ni ratio and mode of preparation. Co-impregnated catalysts exhibit a synergistic effect when a moderate amount of Pt is available: Pt55 Ni45 -CI catalyst was more active than both the pure monometallic catalysts. XRD and SEM equipped with EDSX lead us to believe that alloying occurs in the catalyst. Furthermore, surface segregation of Pt on the alloys as proven by XPS also contributes to this enhanced reactivity. In contrast to co-impregnated catalyst, all the step-impregnated catalysts show low catalytic reactivity when compared to pure Pt. [PUBLICATION ABSTRACT]
Pt/Ni–silica catalysts were prepared via co and step impregnation using NaBH 4 as a reducing agent. Pt 55Ni 45-CI (co-impregnated) exhibited superior reactivity compared to the monometallic catalysts. Alloying and Pt segregation may contribute to this enhanced activity. Pt/Ni supported on silica catalysts were synthesized via co-impregnation (CI) and step-impregnation (SI) techniques using NaBH 4 as the metal ions reducing agent. They were characterized by H 2-TPR and H 2-TPD, XRD, TEM, SEM and EDSX analyses as well as tested for the hydrogenation of benzene. The preparation method employed facilitates the formation of totally reduced pure metal or bimetallic metal particles on the surface and catalytic properties are governed by both the Pt/Ni ratio and mode of preparation. Co-impregnated catalysts exhibit a synergistic effect when a moderate amount of Pt is available: Pt 55Ni 45-CI catalyst was more active than both the pure monometallic catalysts. XRD and SEM equipped with EDSX lead us to believe that alloying occurs in the catalyst. Furthermore, surface segregation of Pt on the alloys as proven by XPS also contributes to this enhanced reactivity. In contrast to co-impregnated catalyst, all the step-impregnated catalysts show low catalytic reactivity when compared to pure Pt.
Author Alnot, M.
Abu Bakar, N.H.H.
Abu Bakar, M.
Monteverdi, S.
Bettahar, M.M.
Ismail, J.
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Issue 1
Keywords Impregnation technique
Silica support
Hydrogenation of benzene
Pt/Ni bimetallic nanoparticles
Binary compound
Support
Nanoparticle
Surface segregation
Metal ion
X ray
Hydrogenation
Silica
Supported catalyst
Chemical reduction
Surface properties
Photoelectron spectrometry
Chemical reactivity
Scanning electron microscopy
Catalytic reaction
Metal particle
X ray diffraction
Heterogeneous catalysis
Impregnation
Transmission electron microscopy
Benzene
Preparation
Alloying
Catalyst
Language English
License CC BY 4.0
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Snippet Pt/Ni–silica catalysts were prepared via co and step impregnation using NaBH 4 as a reducing agent. Pt 55Ni 45-CI (co-impregnated) exhibited superior...
Pt/Ni-silica catalysts were prepared via co and step impregnation using NaBH4 as a reducing agent. Pt55 Ni45 -CI (co-impregnated) exhibited superior reactivity...
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StartPage 63
SubjectTerms Catalysis
Catalysts
Chemistry
Colloidal state and disperse state
Exact sciences and technology
General and physical chemistry
Hydrocarbons
Hydrogenation
Hydrogenation of benzene
Impregnation technique
Metals
Physical and chemical studies. Granulometry. Electrokinetic phenomena
Pt/Ni bimetallic nanoparticles
Silica support
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
Title PtNi catalysts prepared via borohydride reduction for hydrogenation of benzene
URI https://dx.doi.org/10.1016/j.jcat.2009.04.011
https://www.proquest.com/docview/195455242
Volume 265
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