Serveur d'exploration sur le nickel au Maghreb

Attention, ce site est en cours de développement !
Attention, site généré par des moyens informatiques à partir de corpus bruts.
Les informations ne sont donc pas validées.

Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts

Identifieur interne : 000422 ( Main/Exploration ); précédent : 000421; suivant : 000423

Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts

Auteurs : Yacine Rezgui [Algérie] ; Miloud Guemini [Algérie]

Source :

RBID : Pascal:10-0288962

Descripteurs français

English descriptors

Abstract

A series of NiPtW/silica-alumina catalysts (wt.%: Ni,12-17; W: 10, Pt: 0.1-1) were prepared via a hybrid method: sol-gel and incipient wetness impregnation and characterized by inductively coupled plasma-atomic emission spectroscopy (ICP-AES), BET, temperature-programmed desorption of ammonia (NH3-TPD), pyridine adsorption followed by FTIR and TPO techniques. On these catalysts, n-decane hydroisomerization was carried out under the following conditions: fixed bed reactor, atmospheric pressure, temperature ranging from 150 to 300 °C, weight hourly space velocity of 4 h-1 and molar hydrogen/hydrocarbon ratio of 5. Pt was found to promote activity and stability, the effect being optimal for 0.2 wt.% Pt. Isomers and cracking products yields were a function of both metal (Ni and Pt) content and conversion. Whatever n-decane conversion, monobranched isomers were found to be predominant. Besides, up to 10% conversion, the cracked products were not produced in significant amounts. For a time on stream of 100 min, the best results (47% conversion and 56% isomerization selectivity) were obtained at 250 °C over the catalyst containing 12% Ni, 10% W and 0.2% Pt).


Affiliations:


Links toward previous steps (curation, corpus...)


Le document en format XML

<record>
<TEI>
<teiHeader>
<fileDesc>
<titleStmt>
<title xml:lang="en" level="a">Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts</title>
<author>
<name sortKey="Rezgui, Yacine" sort="Rezgui, Yacine" uniqKey="Rezgui Y" first="Yacine" last="Rezgui">Yacine Rezgui</name>
<affiliation wicri:level="1">
<inist:fA14 i1="01">
<s1>Laboratoire de Recherche de Chimie Appliquée et Technologie des Matériaux, Department of Chemistry, Université d'Oum El Bouaghi, B.P. 358, Route de Constantine</s1>
<s2>Oum El Bouaghi 04000</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<wicri:noRegion>Oum El Bouaghi 04000</wicri:noRegion>
</affiliation>
</author>
<author>
<name sortKey="Guemini, Miloud" sort="Guemini, Miloud" uniqKey="Guemini M" first="Miloud" last="Guemini">Miloud Guemini</name>
<affiliation wicri:level="1">
<inist:fA14 i1="01">
<s1>Laboratoire de Recherche de Chimie Appliquée et Technologie des Matériaux, Department of Chemistry, Université d'Oum El Bouaghi, B.P. 358, Route de Constantine</s1>
<s2>Oum El Bouaghi 04000</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<wicri:noRegion>Oum El Bouaghi 04000</wicri:noRegion>
</affiliation>
</author>
</titleStmt>
<publicationStmt>
<idno type="wicri:source">INIST</idno>
<idno type="inist">10-0288962</idno>
<date when="2010">2010</date>
<idno type="stanalyst">PASCAL 10-0288962 INIST</idno>
<idno type="RBID">Pascal:10-0288962</idno>
<idno type="wicri:Area/PascalFrancis/Corpus">000154</idno>
<idno type="wicri:Area/PascalFrancis/Curation">000287</idno>
<idno type="wicri:Area/PascalFrancis/Checkpoint">000150</idno>
<idno type="wicri:explorRef" wicri:stream="PascalFrancis" wicri:step="Checkpoint">000150</idno>
<idno type="wicri:doubleKey">0926-860X:2010:Rezgui Y:hydroisomerization:of:n</idno>
<idno type="wicri:Area/Main/Merge">000433</idno>
<idno type="wicri:Area/Main/Curation">000422</idno>
<idno type="wicri:Area/Main/Exploration">000422</idno>
</publicationStmt>
<sourceDesc>
<biblStruct>
<analytic>
<title xml:lang="en" level="a">Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts</title>
<author>
<name sortKey="Rezgui, Yacine" sort="Rezgui, Yacine" uniqKey="Rezgui Y" first="Yacine" last="Rezgui">Yacine Rezgui</name>
<affiliation wicri:level="1">
<inist:fA14 i1="01">
<s1>Laboratoire de Recherche de Chimie Appliquée et Technologie des Matériaux, Department of Chemistry, Université d'Oum El Bouaghi, B.P. 358, Route de Constantine</s1>
<s2>Oum El Bouaghi 04000</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<wicri:noRegion>Oum El Bouaghi 04000</wicri:noRegion>
</affiliation>
</author>
<author>
<name sortKey="Guemini, Miloud" sort="Guemini, Miloud" uniqKey="Guemini M" first="Miloud" last="Guemini">Miloud Guemini</name>
<affiliation wicri:level="1">
<inist:fA14 i1="01">
<s1>Laboratoire de Recherche de Chimie Appliquée et Technologie des Matériaux, Department of Chemistry, Université d'Oum El Bouaghi, B.P. 358, Route de Constantine</s1>
<s2>Oum El Bouaghi 04000</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
</inist:fA14>
<country>Algérie</country>
<wicri:noRegion>Oum El Bouaghi 04000</wicri:noRegion>
</affiliation>
</author>
</analytic>
<series>
<title level="j" type="main">Applied catalysis. A, General : (Print)</title>
<title level="j" type="abbreviated">Appl. catal., A Gen. : (Print)</title>
<idno type="ISSN">0926-860X</idno>
<imprint>
<date when="2010">2010</date>
</imprint>
</series>
</biblStruct>
</sourceDesc>
<seriesStmt>
<title level="j" type="main">Applied catalysis. A, General : (Print)</title>
<title level="j" type="abbreviated">Appl. catal., A Gen. : (Print)</title>
<idno type="ISSN">0926-860X</idno>
</seriesStmt>
</fileDesc>
<profileDesc>
<textClass>
<keywords scheme="KwdEn" xml:lang="en">
<term>Adsorption</term>
<term>Alumina</term>
<term>Ammonia</term>
<term>Atmospheric pressure</term>
<term>Catalyst</term>
<term>Conversion</term>
<term>Decane</term>
<term>Fixed bed reactor</term>
<term>Heterogeneous catalysis</term>
<term>Hydrocarbon</term>
<term>Hydrogen</term>
<term>Impregnation</term>
<term>Infrared spectrometry</term>
<term>Isomer</term>
<term>Isomerization</term>
<term>Nickel</term>
<term>Plasma</term>
<term>Platinum</term>
<term>Pyridine</term>
<term>Selectivity</term>
<term>Silica</term>
<term>Sol gel process</term>
<term>Stability</term>
<term>Support</term>
<term>Thermodesorption</term>
<term>Velocity</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr">
<term>Décane</term>
<term>Support</term>
<term>Silice</term>
<term>Alumine</term>
<term>Catalyseur</term>
<term>Platine</term>
<term>Nickel</term>
<term>Isomérisation</term>
<term>Stabilité</term>
<term>Catalyse hétérogène</term>
<term>Procédé sol gel</term>
<term>Imprégnation</term>
<term>Plasma</term>
<term>Thermodésorption</term>
<term>Ammoniac</term>
<term>Pyridine</term>
<term>Adsorption</term>
<term>Spectrométrie IR</term>
<term>Réacteur lit fixe</term>
<term>Pression atmosphérique</term>
<term>Vitesse</term>
<term>Hydrogène</term>
<term>Hydrocarbure</term>
<term>Isomère</term>
<term>Conversion</term>
<term>Sélectivité</term>
<term>SiO2</term>
<term>Al2O3</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr">
<term>Platine</term>
<term>Nickel</term>
<term>Hydrogène</term>
<term>Hydrocarbure</term>
</keywords>
</textClass>
</profileDesc>
</teiHeader>
<front>
<div type="abstract" xml:lang="en">A series of NiPtW/silica-alumina catalysts (wt.%: Ni,12-17; W: 10, Pt: 0.1-1) were prepared via a hybrid method: sol-gel and incipient wetness impregnation and characterized by inductively coupled plasma-atomic emission spectroscopy (ICP-AES), BET, temperature-programmed desorption of ammonia (NH
<sub>3</sub>
-TPD), pyridine adsorption followed by FTIR and TPO techniques. On these catalysts, n-decane hydroisomerization was carried out under the following conditions: fixed bed reactor, atmospheric pressure, temperature ranging from 150 to 300 °C, weight hourly space velocity of 4 h
<sup>-1</sup>
and molar hydrogen/hydrocarbon ratio of 5. Pt was found to promote activity and stability, the effect being optimal for 0.2 wt.% Pt. Isomers and cracking products yields were a function of both metal (Ni and Pt) content and conversion. Whatever n-decane conversion, monobranched isomers were found to be predominant. Besides, up to 10% conversion, the cracked products were not produced in significant amounts. For a time on stream of 100 min, the best results (47% conversion and 56% isomerization selectivity) were obtained at 250 °C over the catalyst containing 12% Ni, 10% W and 0.2% Pt).</div>
</front>
</TEI>
<affiliations>
<list>
<country>
<li>Algérie</li>
</country>
</list>
<tree>
<country name="Algérie">
<noRegion>
<name sortKey="Rezgui, Yacine" sort="Rezgui, Yacine" uniqKey="Rezgui Y" first="Yacine" last="Rezgui">Yacine Rezgui</name>
</noRegion>
<name sortKey="Guemini, Miloud" sort="Guemini, Miloud" uniqKey="Guemini M" first="Miloud" last="Guemini">Miloud Guemini</name>
</country>
</tree>
</affiliations>
</record>

Pour manipuler ce document sous Unix (Dilib)

EXPLOR_STEP=$WICRI_ROOT/Wicri/Terre/explor/NickelMaghrebV1/Data/Main/Exploration
HfdSelect -h $EXPLOR_STEP/biblio.hfd -nk 000422 | SxmlIndent | more

Ou

HfdSelect -h $EXPLOR_AREA/Data/Main/Exploration/biblio.hfd -nk 000422 | SxmlIndent | more

Pour mettre un lien sur cette page dans le réseau Wicri

{{Explor lien
   |wiki=    Wicri/Terre
   |area=    NickelMaghrebV1
   |flux=    Main
   |étape=   Exploration
   |type=    RBID
   |clé=     Pascal:10-0288962
   |texte=   Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts
}}

Wicri

This area was generated with Dilib version V0.6.27.
Data generation: Fri Mar 24 23:14:20 2017. Site generation: Tue Mar 5 17:03:47 2024