NickelMaghrebV1, PascalFrancis, Curation, bibRecord, 000287

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

Identifieur interne : 000287 ( PascalFrancis/Curation ); précédent : 000286; suivant : 000288

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

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

Source :

Applied catalysis. A, General : (Print) [ 0926-860X ] ; 2010.

RBID : Pascal:10-0288962

Descripteurs français

Pascal (Inist)
- Décane, Support, Silice, Alumine, Catalyseur, Platine, Nickel, Isomérisation, Stabilité, Catalyse hétérogène, Procédé sol gel, Imprégnation, Plasma, Thermodésorption, Ammoniac, Pyridine, Adsorption, Spectrométrie IR, Réacteur lit fixe, Pression atmosphérique, Vitesse, Hydrogène, Hydrocarbure, Isomère, Conversion, Sélectivité, SiO2, Al2O3.
Wicri :
- topic : Platine, Nickel, Hydrogène, Hydrocarbure.

English descriptors

KwdEn :
- Adsorption, Alumina, Ammonia, Atmospheric pressure, Catalyst, Conversion, Decane, Fixed bed reactor, Heterogeneous catalysis, Hydrocarbon, Hydrogen, Impregnation, Infrared spectrometry, Isomer, Isomerization, Nickel, Plasma, Platinum, Pyridine, Selectivity, Silica, Sol gel process, Stability, Support, Thermodesorption, Velocity.

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).

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A03		`1`		`@0 Appl. catal., A Gen. : (Print)`
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A08	`01`	`1`	`ENG`	`@1 Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts`
A11	`01`	`1`		`@1 REZGUI (Yacine)`
A11	`02`	`1`		`@1 GUEMINI (Miloud)`
A14	`01`			`@1 Laboratoire de Recherche de Chimie Appliquée et Technologie des Matériaux, Department of Chemistry, Université d'Oum El Bouaghi, B.P. 358, Route de Constantine @2 Oum El Bouaghi 04000 @3 DZA @Z 1 aut. @Z 2 aut.`
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A23	`01`			`@0 ENG`
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A44				`@0 0000 @1 © 2010 INIST-CNRS. All rights reserved.`
A45				`@0 49 ref.`
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C01	`01`		`ENG`	@0 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).
C02	`01`	`X`		`@0 001C01A03`
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C02	`03`	`X`		`@0 001C01I`
C03	`01`	`X`	`FRE`	`@0 Décane @2 NK @5 01`
C03	`01`	`X`	`ENG`	`@0 Decane @2 NK @5 01`
C03	`01`	`X`	`SPA`	`@0 Decano @2 NK @5 01`
C03	`02`	`X`	`FRE`	`@0 Support @5 02`
C03	`02`	`X`	`ENG`	`@0 Support @5 02`
C03	`02`	`X`	`SPA`	`@0 Soporte @5 02`
C03	`03`	`X`	`FRE`	`@0 Silice @2 NK @2 FX @5 03`
C03	`03`	`X`	`ENG`	`@0 Silica @2 NK @2 FX @5 03`
C03	`03`	`X`	`SPA`	`@0 Sílice @2 NK @2 FX @5 03`
C03	`04`	`X`	`FRE`	`@0 Alumine @2 NK @5 04`
C03	`04`	`X`	`ENG`	`@0 Alumina @2 NK @5 04`
C03	`04`	`X`	`SPA`	`@0 Alúmina @2 NK @5 04`
C03	`05`	`X`	`FRE`	`@0 Catalyseur @5 05`
C03	`05`	`X`	`ENG`	`@0 Catalyst @5 05`
C03	`05`	`X`	`SPA`	`@0 Catalizador @5 05`
C03	`06`	`X`	`FRE`	`@0 Platine @2 NC @5 06`
C03	`06`	`X`	`ENG`	`@0 Platinum @2 NC @5 06`
C03	`06`	`X`	`SPA`	`@0 Platino @2 NC @5 06`
C03	`07`	`X`	`FRE`	`@0 Nickel @2 NC @2 FX @5 07`
C03	`07`	`X`	`ENG`	`@0 Nickel @2 NC @2 FX @5 07`
C03	`07`	`X`	`SPA`	`@0 Niquel @2 NC @2 FX @5 07`
C03	`08`	`X`	`FRE`	`@0 Isomérisation @5 08`
C03	`08`	`X`	`ENG`	`@0 Isomerization @5 08`
C03	`08`	`X`	`SPA`	`@0 Isomerización @5 08`
C03	`09`	`X`	`FRE`	`@0 Stabilité @5 09`
C03	`09`	`X`	`ENG`	`@0 Stability @5 09`
C03	`09`	`X`	`SPA`	`@0 Estabilidad @5 09`
C03	`10`	`X`	`FRE`	`@0 Catalyse hétérogène @5 10`
C03	`10`	`X`	`ENG`	`@0 Heterogeneous catalysis @5 10`
C03	`10`	`X`	`SPA`	`@0 Catálisis heterogénea @5 10`
C03	`11`	`X`	`FRE`	`@0 Procédé sol gel @5 13`
C03	`11`	`X`	`ENG`	`@0 Sol gel process @5 13`
C03	`11`	`X`	`SPA`	`@0 Procedimiento sol gel @5 13`
C03	`12`	`X`	`FRE`	`@0 Imprégnation @5 14`
C03	`12`	`X`	`ENG`	`@0 Impregnation @5 14`
C03	`12`	`X`	`SPA`	`@0 Impregnación @5 14`
C03	`13`	`X`	`FRE`	`@0 Plasma @5 15`
C03	`13`	`X`	`ENG`	`@0 Plasma @5 15`
C03	`13`	`X`	`SPA`	`@0 Plasma @5 15`
C03	`14`	`X`	`FRE`	`@0 Thermodésorption @5 16`
C03	`14`	`X`	`ENG`	`@0 Thermodesorption @5 16`
C03	`14`	`X`	`SPA`	`@0 Desabsorción térmica @5 16`
C03	`15`	`X`	`FRE`	`@0 Ammoniac @2 NK @2 FX @5 17`
C03	`15`	`X`	`ENG`	`@0 Ammonia @2 NK @2 FX @5 17`
C03	`15`	`X`	`SPA`	`@0 Amoníaco @2 NK @2 FX @5 17`
C03	`16`	`X`	`FRE`	`@0 Pyridine @2 NK @5 18`
C03	`16`	`X`	`ENG`	`@0 Pyridine @2 NK @5 18`
C03	`16`	`X`	`SPA`	`@0 Piridina @2 NK @5 18`
C03	`17`	`X`	`FRE`	`@0 Adsorption @5 19`
C03	`17`	`X`	`ENG`	`@0 Adsorption @5 19`
C03	`17`	`X`	`SPA`	`@0 Adsorción @5 19`
C03	`18`	`X`	`FRE`	`@0 Spectrométrie IR @5 20`
C03	`18`	`X`	`ENG`	`@0 Infrared spectrometry @5 20`
C03	`18`	`X`	`SPA`	`@0 Espectrometría IR @5 20`
C03	`19`	`X`	`FRE`	`@0 Réacteur lit fixe @5 21`
C03	`19`	`X`	`ENG`	`@0 Fixed bed reactor @5 21`
C03	`19`	`X`	`SPA`	`@0 Reactor lecho fijo @5 21`
C03	`20`	`X`	`FRE`	`@0 Pression atmosphérique @5 22`
C03	`20`	`X`	`ENG`	`@0 Atmospheric pressure @5 22`
C03	`20`	`X`	`SPA`	`@0 Presión atmosférica @5 22`
C03	`21`	`X`	`FRE`	`@0 Vitesse @5 23`
C03	`21`	`X`	`ENG`	`@0 Velocity @5 23`
C03	`21`	`X`	`SPA`	`@0 Velocidad @5 23`
C03	`22`	`X`	`FRE`	`@0 Hydrogène @2 NC @5 24`
C03	`22`	`X`	`ENG`	`@0 Hydrogen @2 NC @5 24`
C03	`22`	`X`	`SPA`	`@0 Hidrógeno @2 NC @5 24`
C03	`23`	`X`	`FRE`	`@0 Hydrocarbure @2 FX @5 25`
C03	`23`	`X`	`ENG`	`@0 Hydrocarbon @2 FX @5 25`
C03	`23`	`X`	`SPA`	`@0 Hidrocarburo @2 FX @5 25`
C03	`24`	`X`	`FRE`	`@0 Isomère @5 26`
C03	`24`	`X`	`ENG`	`@0 Isomer @5 26`
C03	`24`	`X`	`SPA`	`@0 Isómero @5 26`
C03	`25`	`X`	`FRE`	`@0 Conversion @5 27`
C03	`25`	`X`	`ENG`	`@0 Conversion @5 27`
C03	`25`	`X`	`SPA`	`@0 Conversión @5 27`
C03	`26`	`X`	`FRE`	`@0 Sélectivité @5 28`
C03	`26`	`X`	`ENG`	`@0 Selectivity @5 28`
C03	`26`	`X`	`SPA`	`@0 Selectividad @5 28`
C03	`27`	`X`	`FRE`	`@0 SiO2 @4 INC @5 32`
C03	`28`	`X`	`FRE`	`@0 Al2O3 @4 INC @5 33`
C07	`01`	`X`	`FRE`	`@0 Composé binaire @5 11`
C07	`01`	`X`	`ENG`	`@0 Binary compound @5 11`
C07	`01`	`X`	`SPA`	`@0 Compuesto binario @5 11`
C07	`02`	`X`	`FRE`	`@0 Métal transition @2 NC @5 12`
C07	`02`	`X`	`ENG`	`@0 Transition metal @2 NC @5 12`
C07	`02`	`X`	`SPA`	`@0 Metal transición @2 NC @5 12`
C07	`03`	`X`	`FRE`	`@0 Hétérocycle azote @5 29`
C07	`03`	`X`	`ENG`	`@0 Nitrogen heterocycle @5 29`
C07	`03`	`X`	`SPA`	`@0 Heterociclo nitrógeno @5 29`
C07	`04`	`X`	`FRE`	`@0 Cycle 6 chaînons @5 30`
C07	`04`	`X`	`ENG`	`@0 Six membered ring @5 30`
C07	`04`	`X`	`SPA`	`@0 Ciclo 6 eslabones @5 30`
N21				`@1 186`
N44	`01`			`@1 OTO`
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Le document en format XML

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<term>Alumina</term>
<term>Ammonia</term>
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<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>
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<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>
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<term>Nickel</term>
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<term>Catalyse hétérogène</term>
<term>Procédé sol gel</term>
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<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>
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<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>
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<fC01 i1="01" l="ENG"><s0>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).</s0>
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<fC03 i1="01" i2="X" l="FRE"><s0>Décane</s0>
<s2>NK</s2>
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<fC03 i1="01" i2="X" l="ENG"><s0>Decane</s0>
<s2>NK</s2>
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<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Support</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Soporte</s0>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Silice</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Silica</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Sílice</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Alumine</s0>
<s2>NK</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Alumina</s0>
<s2>NK</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Alúmina</s0>
<s2>NK</s2>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Catalyseur</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Catalyst</s0>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Catalizador</s0>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Platine</s0>
<s2>NC</s2>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Platinum</s0>
<s2>NC</s2>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Platino</s0>
<s2>NC</s2>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Nickel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Nickel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Niquel</s0>
<s2>NC</s2>
<s2>FX</s2>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Isomérisation</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Isomerization</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Isomerización</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Stabilité</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Stability</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Estabilidad</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Catalyse hétérogène</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Heterogeneous catalysis</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Catálisis heterogénea</s0>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Procédé sol gel</s0>
<s5>13</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Sol gel process</s0>
<s5>13</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Procedimiento sol gel</s0>
<s5>13</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Imprégnation</s0>
<s5>14</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Impregnation</s0>
<s5>14</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Impregnación</s0>
<s5>14</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Plasma</s0>
<s5>15</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Plasma</s0>
<s5>15</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Plasma</s0>
<s5>15</s5>
</fC03>
<fC03 i1="14" i2="X" l="FRE"><s0>Thermodésorption</s0>
<s5>16</s5>
</fC03>
<fC03 i1="14" i2="X" l="ENG"><s0>Thermodesorption</s0>
<s5>16</s5>
</fC03>
<fC03 i1="14" i2="X" l="SPA"><s0>Desabsorción térmica</s0>
<s5>16</s5>
</fC03>
<fC03 i1="15" i2="X" l="FRE"><s0>Ammoniac</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>17</s5>
</fC03>
<fC03 i1="15" i2="X" l="ENG"><s0>Ammonia</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>17</s5>
</fC03>
<fC03 i1="15" i2="X" l="SPA"><s0>Amoníaco</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>17</s5>
</fC03>
<fC03 i1="16" i2="X" l="FRE"><s0>Pyridine</s0>
<s2>NK</s2>
<s5>18</s5>
</fC03>
<fC03 i1="16" i2="X" l="ENG"><s0>Pyridine</s0>
<s2>NK</s2>
<s5>18</s5>
</fC03>
<fC03 i1="16" i2="X" l="SPA"><s0>Piridina</s0>
<s2>NK</s2>
<s5>18</s5>
</fC03>
<fC03 i1="17" i2="X" l="FRE"><s0>Adsorption</s0>
<s5>19</s5>
</fC03>
<fC03 i1="17" i2="X" l="ENG"><s0>Adsorption</s0>
<s5>19</s5>
</fC03>
<fC03 i1="17" i2="X" l="SPA"><s0>Adsorción</s0>
<s5>19</s5>
</fC03>
<fC03 i1="18" i2="X" l="FRE"><s0>Spectrométrie IR</s0>
<s5>20</s5>
</fC03>
<fC03 i1="18" i2="X" l="ENG"><s0>Infrared spectrometry</s0>
<s5>20</s5>
</fC03>
<fC03 i1="18" i2="X" l="SPA"><s0>Espectrometría IR</s0>
<s5>20</s5>
</fC03>
<fC03 i1="19" i2="X" l="FRE"><s0>Réacteur lit fixe</s0>
<s5>21</s5>
</fC03>
<fC03 i1="19" i2="X" l="ENG"><s0>Fixed bed reactor</s0>
<s5>21</s5>
</fC03>
<fC03 i1="19" i2="X" l="SPA"><s0>Reactor lecho fijo</s0>
<s5>21</s5>
</fC03>
<fC03 i1="20" i2="X" l="FRE"><s0>Pression atmosphérique</s0>
<s5>22</s5>
</fC03>
<fC03 i1="20" i2="X" l="ENG"><s0>Atmospheric pressure</s0>
<s5>22</s5>
</fC03>
<fC03 i1="20" i2="X" l="SPA"><s0>Presión atmosférica</s0>
<s5>22</s5>
</fC03>
<fC03 i1="21" i2="X" l="FRE"><s0>Vitesse</s0>
<s5>23</s5>
</fC03>
<fC03 i1="21" i2="X" l="ENG"><s0>Velocity</s0>
<s5>23</s5>
</fC03>
<fC03 i1="21" i2="X" l="SPA"><s0>Velocidad</s0>
<s5>23</s5>
</fC03>
<fC03 i1="22" i2="X" l="FRE"><s0>Hydrogène</s0>
<s2>NC</s2>
<s5>24</s5>
</fC03>
<fC03 i1="22" i2="X" l="ENG"><s0>Hydrogen</s0>
<s2>NC</s2>
<s5>24</s5>
</fC03>
<fC03 i1="22" i2="X" l="SPA"><s0>Hidrógeno</s0>
<s2>NC</s2>
<s5>24</s5>
</fC03>
<fC03 i1="23" i2="X" l="FRE"><s0>Hydrocarbure</s0>
<s2>FX</s2>
<s5>25</s5>
</fC03>
<fC03 i1="23" i2="X" l="ENG"><s0>Hydrocarbon</s0>
<s2>FX</s2>
<s5>25</s5>
</fC03>
<fC03 i1="23" i2="X" l="SPA"><s0>Hidrocarburo</s0>
<s2>FX</s2>
<s5>25</s5>
</fC03>
<fC03 i1="24" i2="X" l="FRE"><s0>Isomère</s0>
<s5>26</s5>
</fC03>
<fC03 i1="24" i2="X" l="ENG"><s0>Isomer</s0>
<s5>26</s5>
</fC03>
<fC03 i1="24" i2="X" l="SPA"><s0>Isómero</s0>
<s5>26</s5>
</fC03>
<fC03 i1="25" i2="X" l="FRE"><s0>Conversion</s0>
<s5>27</s5>
</fC03>
<fC03 i1="25" i2="X" l="ENG"><s0>Conversion</s0>
<s5>27</s5>
</fC03>
<fC03 i1="25" i2="X" l="SPA"><s0>Conversión</s0>
<s5>27</s5>
</fC03>
<fC03 i1="26" i2="X" l="FRE"><s0>Sélectivité</s0>
<s5>28</s5>
</fC03>
<fC03 i1="26" i2="X" l="ENG"><s0>Selectivity</s0>
<s5>28</s5>
</fC03>
<fC03 i1="26" i2="X" l="SPA"><s0>Selectividad</s0>
<s5>28</s5>
</fC03>
<fC03 i1="27" i2="X" l="FRE"><s0>SiO2</s0>
<s4>INC</s4>
<s5>32</s5>
</fC03>
<fC03 i1="28" i2="X" l="FRE"><s0>Al2O3</s0>
<s4>INC</s4>
<s5>33</s5>
</fC03>
<fC07 i1="01" i2="X" l="FRE"><s0>Composé binaire</s0>
<s5>11</s5>
</fC07>
<fC07 i1="01" i2="X" l="ENG"><s0>Binary compound</s0>
<s5>11</s5>
</fC07>
<fC07 i1="01" i2="X" l="SPA"><s0>Compuesto binario</s0>
<s5>11</s5>
</fC07>
<fC07 i1="02" i2="X" l="FRE"><s0>Métal transition</s0>
<s2>NC</s2>
<s5>12</s5>
</fC07>
<fC07 i1="02" i2="X" l="ENG"><s0>Transition metal</s0>
<s2>NC</s2>
<s5>12</s5>
</fC07>
<fC07 i1="02" i2="X" l="SPA"><s0>Metal transición</s0>
<s2>NC</s2>
<s5>12</s5>
</fC07>
<fC07 i1="03" i2="X" l="FRE"><s0>Hétérocycle azote</s0>
<s5>29</s5>
</fC07>
<fC07 i1="03" i2="X" l="ENG"><s0>Nitrogen heterocycle</s0>
<s5>29</s5>
</fC07>
<fC07 i1="03" i2="X" l="SPA"><s0>Heterociclo nitrógeno</s0>
<s5>29</s5>
</fC07>
<fC07 i1="04" i2="X" l="FRE"><s0>Cycle 6 chaînons</s0>
<s5>30</s5>
</fC07>
<fC07 i1="04" i2="X" l="ENG"><s0>Six membered ring</s0>
<s5>30</s5>
</fC07>
<fC07 i1="04" i2="X" l="SPA"><s0>Ciclo 6 eslabones</s0>
<s5>30</s5>
</fC07>
<fN21><s1>186</s1>
</fN21>
<fN44 i1="01"><s1>OTO</s1>
</fN44>
<fN82><s1>OTO</s1>
</fN82>
</pA>
</standard>
</inist>
</record>

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   |wiki=    Wicri/Terre
   |area=    NickelMaghrebV1
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   |texte=   Hydroisomerization of n-decane over Ni-Pt-W supported on amorphous silica-alumina catalysts
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Data generation: Fri Mar 24 23:14:20 2017. Site generation: Tue Mar 5 17:03:47 2024

	Serveur d'exploration sur le nickel au Maghreb
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Serveur d'exploration sur le nickel au Maghreb

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

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

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