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 : 000964Isomerization 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 :
- Catalysis letters [ 1011-372X ] ; 2003.
Descripteurs français
- Pascal (Inist)
- Wicri :
- topic : Nickel.
English descriptors
- KwdEn :
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.
Affiliations:
Links toward previous steps (curation, corpus...)
- to stream PascalFrancis, to step Corpus: 000376
- to stream PascalFrancis, to step Curation: 000065
- to stream PascalFrancis, to step Checkpoint: 000368
- to stream Main, to step Merge: 000986
- to stream Main, to step Curation: 000963
Le document en format XML
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/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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<sourceDesc><biblStruct><analytic><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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<country>Algérie</country>
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<author><name sortKey="Guemini, M" sort="Guemini, M" uniqKey="Guemini M" first="M." last="Guemini">M. Guemini</name>
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<author><name sortKey="Tighezza, A" sort="Tighezza, A" uniqKey="Tighezza A" first="A." last="Tighezza">A. Tighezza</name>
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<author><name sortKey="Bouchemma, A" sort="Bouchemma, A" uniqKey="Bouchemma A" first="A." last="Bouchemma">A. Bouchemma</name>
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<series><title level="j" type="main">Catalysis letters</title>
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<imprint><date when="2003">2003</date>
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<seriesStmt><title level="j" type="main">Catalysis letters</title>
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<profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Calcining</term>
<term>Catalytic reaction</term>
<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>
<term>Octane number</term>
<term>Operating conditions</term>
<term>Sol gel process</term>
<term>Supported catalyst</term>
<term>Tungsten Oxides</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Isomérisation</term>
<term>Heptane</term>
<term>Catalyseur sur support</term>
<term>Condition opératoire</term>
<term>Nickel</term>
<term>Tungstène Oxyde</term>
<term>Catalyseur modifié</term>
<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>
<term>O W</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Nickel</term>
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<front><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>
</front>
</TEI>
<affiliations><list><country><li>Algérie</li>
<li>Arabie saoudite</li>
</country>
</list>
<tree><country name="Algérie"><noRegion><name sortKey="Rezgui, Y" sort="Rezgui, Y" uniqKey="Rezgui Y" first="Y." last="Rezgui">Y. Rezgui</name>
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<name sortKey="Bouchemma, A" sort="Bouchemma, A" uniqKey="Bouchemma A" first="A." last="Bouchemma">A. Bouchemma</name>
<name sortKey="Guemini, M" sort="Guemini, M" uniqKey="Guemini M" first="M." last="Guemini">M. Guemini</name>
</country>
<country name="Arabie saoudite"><noRegion><name sortKey="Tighezza, A" sort="Tighezza, A" uniqKey="Tighezza A" first="A." last="Tighezza">A. Tighezza</name>
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