Serveur d'exploration sur le nickel au Maghreb

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Isomerization of n-heptane over Ni-WOx/SiO2-Al2O3 catalysts. Effect of operating conditions, and nickel and tungsten loading

Identifieur interne : 000963 ( Main/Exploration ); précédent : 000962; suivant : 000964

Isomerization of n-heptane over Ni-WOx/SiO2-Al2O3 catalysts. Effect of operating conditions, and nickel and tungsten loading

Auteurs : Y. Rezgui [Algérie] ; M. Guemini [Algérie] ; A. Tighezza [Arabie saoudite] ; A. Bouchemma [Algérie]

Source :

RBID : Pascal:03-0249756

Descripteurs français

English descriptors

Abstract

Isomerization of n-heptane over Ni-WOx/Al2O3-SiO2 catalysts was carried out in a continuous flow fixed-bed reactor under atmospheric pressure. The first part of this study deals with the preparation of two series of catalysts (A and B) by the sol-gel method, while the second part deals with the isomerization ofn-heptane. The principal objective of this study was to choose the catalyst giving the best isomer yield (di-and tri-branched ones) with optimum reaction conditions (reaction temperature, reduction temperature and time on stream). From the results obtained, the optimum nickel content was found to be 15 wt% and it seems that the incorporation of tungsten (B series) leads to a significant enhancement in the activity of the prepared catalysts. After running on stream for 100min, the catalyst with 15% nickel and 10% tungsten (B4 catalyst) gives the best results (29% conversion and 70% selectivity) at 250 C.


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Le document en format XML

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<title xml:lang="en" level="a">Isomerization of n-heptane over Ni-WO
<sub>x</sub>
/SiO
<sub>2</sub>
-Al
<sub>2</sub>
O
<sub>3</sub>
catalysts. Effect of operating conditions, and nickel and tungsten loading</title>
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<term>Calcining</term>
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<term>Chemical reduction</term>
<term>Concentration effect</term>
<term>Heptane</term>
<term>Heterogeneous catalysis</term>
<term>Isomerization</term>
<term>Mixed catalyst</term>
<term>Modified catalyst</term>
<term>Nickel</term>
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<term>Isomérisation</term>
<term>Heptane</term>
<term>Catalyseur sur support</term>
<term>Condition opératoire</term>
<term>Nickel</term>
<term>Tungstène Oxyde</term>
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<term>Catalyseur mixte</term>
<term>Réaction catalytique</term>
<term>Procédé sol gel</term>
<term>Effet concentration</term>
<term>Catalyse hétérogène</term>
<term>Réduction chimique</term>
<term>Calcination</term>
<term>Indice octane</term>
<term>WOx</term>
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<div type="abstract" xml:lang="en">Isomerization of n-heptane over Ni-WO
<sub>x</sub>
/Al
<sub>2</sub>
O
<sub>3</sub>
-SiO
<sub>2</sub>
catalysts was carried out in a continuous flow fixed-bed reactor under atmospheric pressure. The first part of this study deals with the preparation of two series of catalysts (A and B) by the sol-gel method, while the second part deals with the isomerization ofn-heptane. The principal objective of this study was to choose the catalyst giving the best isomer yield (di-and tri-branched ones) with optimum reaction conditions (reaction temperature, reduction temperature and time on stream). From the results obtained, the optimum nickel content was found to be 15 wt% and it seems that the incorporation of tungsten (B series) leads to a significant enhancement in the activity of the prepared catalysts. After running on stream for 100min, the catalyst with 15% nickel and 10% tungsten (B4 catalyst) gives the best results (29% conversion and 70% selectivity) at 250 C.</div>
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