Serveur d'exploration sur le cobalt au Maghreb

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Methane conversion to higher alkanes over ruthenium and cobalt loaded Zr3(PO4)4

Identifieur interne : 000115 ( PascalFrancis/Curation ); précédent : 000114; suivant : 000116

Methane conversion to higher alkanes over ruthenium and cobalt loaded Zr3(PO4)4

Auteurs : N. Cheikhi [Maroc] ; M. Zivad [Maroc]

Source :

RBID : Pascal:05-0363864

Descripteurs français

English descriptors

Abstract

The catalyst Ru-Co/Zr3(PO4)4 was synthesized by impregnation and was tested in the reaction of oligomerization of methane into higher hydrocarbon. The reaction was carried out using a two-steps procedure consisting of: - Methane adsorption. - Hydrogenation of the adsorbed entities and formation of higher hydrocarbons. The production of these alkanes extends from ethane to pentane and could schematically be described by the following pathways: CH4 ⇄ (CHx)ads + (4-X)/2H2 CHx, CHy ⇄ CnHm The results showed that addition of cobalt to ruthenium improved the global activity. This promoter effect was attributed to the synergy brought in by cobalt and to the formation of Ru-CO2+species which are more active than ruthenium alone. These species were identified by EDX-STEM and XPS analyses.
pA  
A01 01  1    @0 1155-4339
A03   1    @0 J. phys., IV
A05       @2 123
A08 01  1  ENG  @1 Methane conversion to higher alkanes over ruthenium and cobalt loaded Zr3(PO4)4
A09 01  1  ENG  @1 REMCES IX: Proceedings of the 9th International Seminar on the Physical Chemistry of Solid State Materials
A11 01  1    @1 CHEIKHI (N.)
A11 02  1    @1 ZIVAD (M.)
A12 01  1    @1 BENLHACHEMI (Abdeljalil) @9 ed.
A12 02  1    @1 BENYAICH (H.) @9 ed.
A12 03  1    @1 BOUABID (Khalid) @9 ed.
A12 04  1    @1 BOUKHARI (A.) @9 ed.
A12 05  1    @1 ELAATMANI (M.) @9 ed.
A12 06  1    @1 ES-SAKHI (B.) @9 ed.
A12 07  1    @1 IHLAL (A.) @9 ed.
A12 08  1    @1 KHAIROUNE (S.) @9 ed.
A12 09  1    @1 MANSOURI (I.) @9 ed.
A12 10  1    @1 NOUNAH (Abderrahman) @9 ed.
A12 11  1    @1 TAHA (Mohamed) @9 ed.
A12 12  1    @1 ZAHIDI (E.) @9 ed.
A14 01      @1 Faculté des Sciences, Laboratoire de Physico-Chimie des Matériaux et Catalyse, Département de Chimie, BP. 1014 @2 Rabat @3 MAR @Z 1 aut. @Z 2 aut.
A15 01      @1 Faculté des Sciences, Cité Dakhla @2 Agadir @3 MAR @Z 1 aut. @Z 3 aut. @Z 11 aut.
A15 02      @1 Ecole Supérieure de Technologie @2 Salé Médina @3 MAR @Z 10 aut.
A18 01  1    @1 IBN ZOHR University. Faculty of Sciences @2 Agadir @3 MAR @9 patr.
A20       @1 301-305
A21       @1 2005
A23 01      @0 ENG
A43 01      @1 INIST @2 125C @5 354000126872900540
A44       @0 0000 @1 © 2005 INIST-CNRS. All rights reserved.
A45       @0 16 ref.
A47 01  1    @0 05-0363864
A60       @1 P @2 C
A61       @0 A
A64 01  1    @0 Journal de physique. IV
A66 01      @0 FRA
C01 01    ENG  @0 The catalyst Ru-Co/Zr3(PO4)4 was synthesized by impregnation and was tested in the reaction of oligomerization of methane into higher hydrocarbon. The reaction was carried out using a two-steps procedure consisting of: - Methane adsorption. - Hydrogenation of the adsorbed entities and formation of higher hydrocarbons. The production of these alkanes extends from ethane to pentane and could schematically be described by the following pathways: CH4 ⇄ (CHx)ads + (4-X)/2H2 CHx, CHy ⇄ CnHm The results showed that addition of cobalt to ruthenium improved the global activity. This promoter effect was attributed to the synergy brought in by cobalt and to the formation of Ru-CO2+species which are more active than ruthenium alone. These species were identified by EDX-STEM and XPS analyses.
C02 01  X    @0 001C01A03
C03 01  X  FRE  @0 Catalyseur sur support @5 01
C03 01  X  ENG  @0 Supported catalyst @5 01
C03 01  X  SPA  @0 Catalizador sobre soporte @5 01
C03 02  X  FRE  @0 Métal transition @2 NC @5 02
C03 02  X  ENG  @0 Transition metal @2 NC @5 02
C03 02  X  SPA  @0 Metal transición @2 NC @5 02
C03 03  X  FRE  @0 Platinoïde @2 NC @5 03
C03 03  X  ENG  @0 Platinoid @2 NC @5 03
C03 03  X  SPA  @0 Platinoide @2 NC @5 03
C03 04  X  FRE  @0 Zirconium Phosphate @2 NC @2 NA @5 04
C03 04  X  ENG  @0 Zirconium Phosphates @2 NC @2 NA @5 04
C03 04  X  SPA  @0 Zirconio Fosfato @2 NC @2 NA @5 04
C03 05  X  FRE  @0 Ruthénium @2 NC @5 05
C03 05  X  ENG  @0 Ruthenium @2 NC @5 05
C03 05  X  SPA  @0 Rutenio @2 NC @5 05
C03 06  X  FRE  @0 Cobalt @2 NC @5 06
C03 06  X  ENG  @0 Cobalt @2 NC @5 06
C03 06  X  SPA  @0 Cobalto @2 NC @5 06
C03 07  X  FRE  @0 Oligomérisation @5 07
C03 07  X  ENG  @0 Oligomerization @5 07
C03 07  X  SPA  @0 Oligomerización @5 07
C03 08  X  FRE  @0 Méthane @2 NK @2 FX @5 08
C03 08  X  ENG  @0 Methane @2 NK @2 FX @5 08
C03 08  X  SPA  @0 Metano @2 NK @2 FX @5 08
C03 09  X  FRE  @0 Catalyse hétérogène @5 09
C03 09  X  ENG  @0 Heterogeneous catalysis @5 09
C03 09  X  SPA  @0 Catálisis heterogénea @5 09
C03 10  X  FRE  @0 Hydrocarbure @2 FX @5 10
C03 10  X  ENG  @0 Hydrocarbon @2 FX @5 10
C03 10  X  SPA  @0 Hidrocarburo @2 FX @5 10
C03 11  X  FRE  @0 Alcane @5 11
C03 11  X  ENG  @0 Alkane @5 11
C03 11  X  SPA  @0 Alcano @5 11
N21       @1 255
pR  
A30 01  1  ENG  @1 REMCES International Seminar on the Physical Chemistry of Solid State Materials @2 9 @3 Agadir MAR @4 2002-10-30

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Le document en format XML

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<term>Alkane</term>
<term>Cobalt</term>
<term>Heterogeneous catalysis</term>
<term>Hydrocarbon</term>
<term>Methane</term>
<term>Oligomerization</term>
<term>Platinoid</term>
<term>Ruthenium</term>
<term>Supported catalyst</term>
<term>Transition metal</term>
<term>Zirconium Phosphates</term>
</keywords>
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<term>Catalyseur sur support</term>
<term>Métal transition</term>
<term>Platinoïde</term>
<term>Zirconium Phosphate</term>
<term>Ruthénium</term>
<term>Cobalt</term>
<term>Oligomérisation</term>
<term>Méthane</term>
<term>Catalyse hétérogène</term>
<term>Hydrocarbure</term>
<term>Alcane</term>
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<div type="abstract" xml:lang="en">The catalyst Ru-Co/Zr
<sub>3</sub>
(PO
<sub>4</sub>
)
<sub>4</sub>
was synthesized by impregnation and was tested in the reaction of oligomerization of methane into higher hydrocarbon. The reaction was carried out using a two-steps procedure consisting of: - Methane adsorption. - Hydrogenation of the adsorbed entities and formation of higher hydrocarbons. The production of these alkanes extends from ethane to pentane and could schematically be described by the following pathways: CH
<sub>4</sub>
⇄ (CH
<sub>x</sub>
)
<sub>ads</sub>
+ (4-X)/2H
<sub>2</sub>
CH
<sub>x</sub>
, CH
<sub>y</sub>
⇄ C
<sub>n</sub>
H
<sub>m</sub>
The results showed that addition of cobalt to ruthenium improved the global activity. This promoter effect was attributed to the synergy brought in by cobalt and to the formation of Ru-CO
<sup>2+</sup>
species which are more active than ruthenium alone. These species were identified by EDX-STEM and XPS analyses.</div>
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<sub>3</sub>
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<sub>4</sub>
)
<sub>4</sub>
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<s3>MAR</s3>
<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
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<fA15 i1="01">
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<s3>MAR</s3>
<sZ>1 aut.</sZ>
<sZ>3 aut.</sZ>
<sZ>11 aut.</sZ>
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<fA15 i1="02">
<s1>Ecole Supérieure de Technologie</s1>
<s2>Salé Médina</s2>
<s3>MAR</s3>
<sZ>10 aut.</sZ>
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<s1>IBN ZOHR University. Faculty of Sciences</s1>
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<s2>C</s2>
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</fA64>
<fA66 i1="01">
<s0>FRA</s0>
</fA66>
<fC01 i1="01" l="ENG">
<s0>The catalyst Ru-Co/Zr
<sub>3</sub>
(PO
<sub>4</sub>
)
<sub>4</sub>
was synthesized by impregnation and was tested in the reaction of oligomerization of methane into higher hydrocarbon. The reaction was carried out using a two-steps procedure consisting of: - Methane adsorption. - Hydrogenation of the adsorbed entities and formation of higher hydrocarbons. The production of these alkanes extends from ethane to pentane and could schematically be described by the following pathways: CH
<sub>4</sub>
⇄ (CH
<sub>x</sub>
)
<sub>ads</sub>
+ (4-X)/2H
<sub>2</sub>
CH
<sub>x</sub>
, CH
<sub>y</sub>
⇄ C
<sub>n</sub>
H
<sub>m</sub>
The results showed that addition of cobalt to ruthenium improved the global activity. This promoter effect was attributed to the synergy brought in by cobalt and to the formation of Ru-CO
<sup>2+</sup>
species which are more active than ruthenium alone. These species were identified by EDX-STEM and XPS analyses.</s0>
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<fC02 i1="01" i2="X">
<s0>001C01A03</s0>
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<s5>01</s5>
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<s5>01</s5>
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<fC03 i1="01" i2="X" l="SPA">
<s0>Catalizador sobre soporte</s0>
<s5>01</s5>
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<s2>NC</s2>
<s5>02</s5>
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<s0>Transition metal</s0>
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<s5>02</s5>
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<fC03 i1="02" i2="X" l="SPA">
<s0>Metal transición</s0>
<s2>NC</s2>
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<s5>03</s5>
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<fC03 i1="03" i2="X" l="ENG">
<s0>Platinoid</s0>
<s2>NC</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA">
<s0>Platinoide</s0>
<s2>NC</s2>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE">
<s0>Zirconium Phosphate</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG">
<s0>Zirconium Phosphates</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA">
<s0>Zirconio Fosfato</s0>
<s2>NC</s2>
<s2>NA</s2>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE">
<s0>Ruthénium</s0>
<s2>NC</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG">
<s0>Ruthenium</s0>
<s2>NC</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA">
<s0>Rutenio</s0>
<s2>NC</s2>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE">
<s0>Cobalt</s0>
<s2>NC</s2>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG">
<s0>Cobalt</s0>
<s2>NC</s2>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA">
<s0>Cobalto</s0>
<s2>NC</s2>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE">
<s0>Oligomérisation</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG">
<s0>Oligomerization</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA">
<s0>Oligomerización</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE">
<s0>Méthane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG">
<s0>Methane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA">
<s0>Metano</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE">
<s0>Catalyse hétérogène</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG">
<s0>Heterogeneous catalysis</s0>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA">
<s0>Catálisis heterogénea</s0>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE">
<s0>Hydrocarbure</s0>
<s2>FX</s2>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG">
<s0>Hydrocarbon</s0>
<s2>FX</s2>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA">
<s0>Hidrocarburo</s0>
<s2>FX</s2>
<s5>10</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE">
<s0>Alcane</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG">
<s0>Alkane</s0>
<s5>11</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA">
<s0>Alcano</s0>
<s5>11</s5>
</fC03>
<fN21>
<s1>255</s1>
</fN21>
</pA>
<pR>
<fA30 i1="01" i2="1" l="ENG">
<s1>REMCES International Seminar on the Physical Chemistry of Solid State Materials</s1>
<s2>9</s2>
<s3>Agadir MAR</s3>
<s4>2002-10-30</s4>
</fA30>
</pR>
</standard>
</inist>
</record>

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