Effect of the basicity created by La2O3 addition on the catalytic properties of Co(O)/SiO2 in CH4 + CO2 reaction
Identifieur interne :
000122 ( PascalFrancis/Curation );
précédent :
000121;
suivant :
000123
Effect of the basicity created by La2O3 addition on the catalytic properties of Co(O)/SiO2 in CH4 + CO2 reaction
Auteurs : R. Bouarab [
Algérie,
France] ;
O. Cherifi [
Algérie] ;
A. Auroux [
France]
Source :
-
Thermochimica acta [ 0040-6031 ] ; 2005.
RBID : Pascal:06-0041062
Descripteurs français
English descriptors
Abstract
A series of Co(O)/SiO2 catalysts modified by various amounts of La2O3 (5, 10 or 50 wt.%) were synthesized and studied in the reaction of reforming of methane by carbon dioxide to syngas at the temperature of 873 K. The catalysts were prepared by successive incipient wetness impregnation: La2O3-SiO2 supports were first prepared by impregnating silica with La(NO3)3 solutions. After drying and calcining under airflow, samples were then submitted to a second impregnation with Co(NO3)2. The purpose of this work is to study the acid-base property of these catalysts by CO2 adsorption calorimetry at 353 K and to look at their impact on the catalytic property. The amounts of chemisorbed CO2 and the site strength distribution of the basic sites, i.e., the basicity, were shown to be strongly dependent on La2O3 content. The following order of basicity was observed: Co(0)/5 wt.%La2O3-SiO2 < Co(0)/10 wt.%La2O3-SiO2 «Co(O)/50 wt.%La2O3-SiO2. The addition of La2O3 to the Co(O)/SiO2 reference sample revealed a very positive effect on the catalytic stability of catalysts. La2O3 prevented cobalt phase sintering by avoiding particle coalescence.
pA |
A01 | 01 | 1 | | @0 0040-6031 |
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A02 | 01 | | | @0 THACAS |
---|
A03 | | 1 | | @0 Thermochim. acta |
---|
A05 | | | | @2 434 |
---|
A06 | | | | @2 1-2 |
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A08 | 01 | 1 | ENG | @1 Effect of the basicity created by La2O3 addition on the catalytic properties of Co(O)/SiO2 in CH4 + CO2 reaction |
---|
A09 | 01 | 1 | ENG | @1 Calorimetry and Thermal Effects in Catalysis: A Collection of Papers from the Third International Symposium on Calorimetry and Thermal Effects in Catalysis held in Lyon, France, July 6-9, 2004 |
---|
A11 | 01 | 1 | | @1 BOUARAB (R.) |
---|
A11 | 02 | 1 | | @1 CHERIFI (O.) |
---|
A11 | 03 | 1 | | @1 AUROUX (A.) |
---|
A12 | 01 | 1 | | @1 AUROUX (Aline) @9 ed. |
---|
A14 | 01 | | | @1 Département des Sciences Fondamentales, Ecole Nationale Polytechnique, 10 av. Pasteur @2 El Harrach @3 DZA @Z 1 aut. |
---|
A14 | 02 | | | @1 Institut de Recherches sur la Catalyse, CNRS, 2 av. Einstein @2 69626 Villeurbanne @3 FRA @Z 1 aut. @Z 3 aut. |
---|
A14 | 03 | | | @1 Laboratoire de Chimie de Gaz Naturel, Faculté de Chimie, U.S.T.H.B., BP 32 @2 16111 El Alla, Bah Ezzouar @3 DZA @Z 2 aut. |
---|
A15 | 01 | | | @1 CNRS, Institut de Recherches sur la Catalyse, 2 avenue A. Einstein @2 69626 Villeurbanne @3 FRA @Z 1 aut. |
---|
A20 | | | | @1 69-73 |
---|
A21 | | | | @1 2005 |
---|
A23 | 01 | | | @0 ENG |
---|
A43 | 01 | | | @1 INIST @2 14753 @5 354000131483590110 |
---|
A44 | | | | @0 0000 @1 © 2006 INIST-CNRS. All rights reserved. |
---|
A45 | | | | @0 14 ref. |
---|
A47 | 01 | 1 | | @0 06-0041062 |
---|
A60 | | | | @1 P @2 C |
---|
A61 | | | | @0 A |
---|
A64 | 01 | 1 | | @0 Thermochimica acta |
---|
A66 | 01 | | | @0 NLD |
---|
C01 | 01 | | ENG | @0 A series of Co(O)/SiO2 catalysts modified by various amounts of La2O3 (5, 10 or 50 wt.%) were synthesized and studied in the reaction of reforming of methane by carbon dioxide to syngas at the temperature of 873 K. The catalysts were prepared by successive incipient wetness impregnation: La2O3-SiO2 supports were first prepared by impregnating silica with La(NO3)3 solutions. After drying and calcining under airflow, samples were then submitted to a second impregnation with Co(NO3)2. The purpose of this work is to study the acid-base property of these catalysts by CO2 adsorption calorimetry at 353 K and to look at their impact on the catalytic property. The amounts of chemisorbed CO2 and the site strength distribution of the basic sites, i.e., the basicity, were shown to be strongly dependent on La2O3 content. The following order of basicity was observed: Co(0)/5 wt.%La2O3-SiO2 < Co(0)/10 wt.%La2O3-SiO2 «Co(O)/50 wt.%La2O3-SiO2. The addition of La2O3 to the Co(O)/SiO2 reference sample revealed a very positive effect on the catalytic stability of catalysts. La2O3 prevented cobalt phase sintering by avoiding particle coalescence. |
---|
C02 | 01 | X | | @0 001C01A03B |
---|
C03 | 01 | X | FRE | @0 Basicité @5 01 |
---|
C03 | 01 | X | ENG | @0 Alkalinity @5 01 |
---|
C03 | 01 | X | SPA | @0 Alcalinidad @5 01 |
---|
C03 | 02 | X | FRE | @0 Lanthane oxyde @5 02 |
---|
C03 | 02 | X | ENG | @0 Lanthanum oxide @5 02 |
---|
C03 | 02 | X | SPA | @0 Lantano óxido @5 02 |
---|
C03 | 03 | X | FRE | @0 Silice @1 ACT @2 NK @2 FX @5 03 |
---|
C03 | 03 | X | ENG | @0 Silica @1 ACT @2 NK @2 FX @5 03 |
---|
C03 | 03 | X | SPA | @0 Sílice @1 ACT @2 NK @2 FX @5 03 |
---|
C03 | 04 | X | FRE | @0 Carbone dioxyde @2 NK @2 FX @5 04 |
---|
C03 | 04 | X | ENG | @0 Carbon dioxide @2 NK @2 FX @5 04 |
---|
C03 | 04 | X | SPA | @0 Carbono dióxido @2 NK @2 FX @5 04 |
---|
C03 | 05 | X | FRE | @0 Méthane @2 NK @2 FX @5 05 |
---|
C03 | 05 | X | ENG | @0 Methane @2 NK @2 FX @5 05 |
---|
C03 | 05 | X | SPA | @0 Metano @2 NK @2 FX @5 05 |
---|
C03 | 06 | X | FRE | @0 Reformage @5 06 |
---|
C03 | 06 | X | ENG | @0 Reforming @5 06 |
---|
C03 | 06 | X | SPA | @0 Reformación @5 06 |
---|
C03 | 07 | X | FRE | @0 Catalyseur @5 07 |
---|
C03 | 07 | X | ENG | @0 Catalyst @5 07 |
---|
C03 | 07 | X | SPA | @0 Catalizador @5 07 |
---|
C03 | 08 | X | FRE | @0 Additif @5 08 |
---|
C03 | 08 | X | ENG | @0 Additive @5 08 |
---|
C03 | 08 | X | SPA | @0 Aditivo @5 08 |
---|
C03 | 09 | X | FRE | @0 Cobalt Oxyde @1 ACT @2 NC @2 NA @5 09 |
---|
C03 | 09 | X | ENG | @0 Cobalt Oxides @1 ACT @2 NC @2 NA @5 09 |
---|
C03 | 09 | X | SPA | @0 Cobalto Óxido @1 ACT @2 NC @2 NA @5 09 |
---|
C03 | 10 | X | FRE | @0 Activité catalytique @5 10 |
---|
C03 | 10 | X | ENG | @0 Catalyst activity @5 10 |
---|
C03 | 10 | X | SPA | @0 Actividad catalítica @5 10 |
---|
N21 | | | | @1 016 |
---|
|
pR |
A30 | 01 | 1 | ENG | @1 International Symposium on Calorimetry and Thermal Effects in Catalysis @2 3 @3 Lyon FRA @4 2004-07-06 |
---|
|
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Le document en format XML
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O<sub>3</sub>
addition on the catalytic properties of Co(O)/SiO<sub>2</sub>
in CH<sub>4</sub>
+ CO<sub>2</sub>
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<author><name sortKey="Bouarab, R" sort="Bouarab, R" uniqKey="Bouarab R" first="R." last="Bouarab">R. Bouarab</name>
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<sourceDesc><biblStruct><analytic><title xml:lang="en" level="a">Effect of the basicity created by La<sub>2</sub>
O<sub>3</sub>
addition on the catalytic properties of Co(O)/SiO<sub>2</sub>
in CH<sub>4</sub>
+ CO<sub>2</sub>
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<author><name sortKey="Bouarab, R" sort="Bouarab, R" uniqKey="Bouarab R" first="R." last="Bouarab">R. Bouarab</name>
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<author><name sortKey="Cherifi, O" sort="Cherifi, O" uniqKey="Cherifi O" first="O." last="Cherifi">O. Cherifi</name>
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<sZ>3 aut.</sZ>
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<term>Catalyst</term>
<term>Catalyst activity</term>
<term>Cobalt Oxides</term>
<term>Lanthanum oxide</term>
<term>Methane</term>
<term>Reforming</term>
<term>Silica</term>
</keywords>
<keywords scheme="Pascal" xml:lang="fr"><term>Basicité</term>
<term>Lanthane oxyde</term>
<term>Silice</term>
<term>Carbone dioxyde</term>
<term>Méthane</term>
<term>Reformage</term>
<term>Catalyseur</term>
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<front><div type="abstract" xml:lang="en">A series of Co(O)/SiO<sub>2</sub>
catalysts modified by various amounts of La<sub>2</sub>
O<sub>3</sub>
(5, 10 or 50 wt.%) were synthesized and studied in the reaction of reforming of methane by carbon dioxide to syngas at the temperature of 873 K. The catalysts were prepared by successive incipient wetness impregnation: La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
supports were first prepared by impregnating silica with La(NO<sub>3</sub>
)<sub>3</sub>
solutions. After drying and calcining under airflow, samples were then submitted to a second impregnation with Co(NO<sub>3</sub>
)<sub>2</sub>
. The purpose of this work is to study the acid-base property of these catalysts by CO<sub>2</sub>
adsorption calorimetry at 353 K and to look at their impact on the catalytic property. The amounts of chemisorbed CO<sub>2</sub>
and the site strength distribution of the basic sites, i.e., the basicity, were shown to be strongly dependent on La<sub>2</sub>
O<sub>3</sub>
content. The following order of basicity was observed: Co(0)/5 wt.%La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
< Co(0)/10 wt.%La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
«Co(O)/50 wt.%La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
. The addition of La<sub>2</sub>
O<sub>3</sub>
to the Co(O)/SiO<sub>2</sub>
reference sample revealed a very positive effect on the catalytic stability of catalysts. La<sub>2</sub>
O<sub>3</sub>
prevented cobalt phase sintering by avoiding particle coalescence.</div>
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<fA03 i2="1"><s0>Thermochim. acta</s0>
</fA03>
<fA05><s2>434</s2>
</fA05>
<fA06><s2>1-2</s2>
</fA06>
<fA08 i1="01" i2="1" l="ENG"><s1>Effect of the basicity created by La<sub>2</sub>
O<sub>3</sub>
addition on the catalytic properties of Co(O)/SiO<sub>2</sub>
in CH<sub>4</sub>
+ CO<sub>2</sub>
reaction</s1>
</fA08>
<fA09 i1="01" i2="1" l="ENG"><s1>Calorimetry and Thermal Effects in Catalysis: A Collection of Papers from the Third International Symposium on Calorimetry and Thermal Effects in Catalysis held in Lyon, France, July 6-9, 2004</s1>
</fA09>
<fA11 i1="01" i2="1"><s1>BOUARAB (R.)</s1>
</fA11>
<fA11 i1="02" i2="1"><s1>CHERIFI (O.)</s1>
</fA11>
<fA11 i1="03" i2="1"><s1>AUROUX (A.)</s1>
</fA11>
<fA12 i1="01" i2="1"><s1>AUROUX (Aline)</s1>
<s9>ed.</s9>
</fA12>
<fA14 i1="01"><s1>Département des Sciences Fondamentales, Ecole Nationale Polytechnique, 10 av. Pasteur</s1>
<s2>El Harrach</s2>
<s3>DZA</s3>
<sZ>1 aut.</sZ>
</fA14>
<fA14 i1="02"><s1>Institut de Recherches sur la Catalyse, CNRS, 2 av. Einstein</s1>
<s2>69626 Villeurbanne</s2>
<s3>FRA</s3>
<sZ>1 aut.</sZ>
<sZ>3 aut.</sZ>
</fA14>
<fA14 i1="03"><s1>Laboratoire de Chimie de Gaz Naturel, Faculté de Chimie, U.S.T.H.B., BP 32</s1>
<s2>16111 El Alla, Bah Ezzouar</s2>
<s3>DZA</s3>
<sZ>2 aut.</sZ>
</fA14>
<fA15 i1="01"><s1>CNRS, Institut de Recherches sur la Catalyse, 2 avenue A. Einstein</s1>
<s2>69626 Villeurbanne</s2>
<s3>FRA</s3>
<sZ>1 aut.</sZ>
</fA15>
<fA20><s1>69-73</s1>
</fA20>
<fA21><s1>2005</s1>
</fA21>
<fA23 i1="01"><s0>ENG</s0>
</fA23>
<fA43 i1="01"><s1>INIST</s1>
<s2>14753</s2>
<s5>354000131483590110</s5>
</fA43>
<fA44><s0>0000</s0>
<s1>© 2006 INIST-CNRS. All rights reserved.</s1>
</fA44>
<fA45><s0>14 ref.</s0>
</fA45>
<fA47 i1="01" i2="1"><s0>06-0041062</s0>
</fA47>
<fA60><s1>P</s1>
<s2>C</s2>
</fA60>
<fA64 i1="01" i2="1"><s0>Thermochimica acta</s0>
</fA64>
<fA66 i1="01"><s0>NLD</s0>
</fA66>
<fC01 i1="01" l="ENG"><s0>A series of Co(O)/SiO<sub>2</sub>
catalysts modified by various amounts of La<sub>2</sub>
O<sub>3</sub>
(5, 10 or 50 wt.%) were synthesized and studied in the reaction of reforming of methane by carbon dioxide to syngas at the temperature of 873 K. The catalysts were prepared by successive incipient wetness impregnation: La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
supports were first prepared by impregnating silica with La(NO<sub>3</sub>
)<sub>3</sub>
solutions. After drying and calcining under airflow, samples were then submitted to a second impregnation with Co(NO<sub>3</sub>
)<sub>2</sub>
. The purpose of this work is to study the acid-base property of these catalysts by CO<sub>2</sub>
adsorption calorimetry at 353 K and to look at their impact on the catalytic property. The amounts of chemisorbed CO<sub>2</sub>
and the site strength distribution of the basic sites, i.e., the basicity, were shown to be strongly dependent on La<sub>2</sub>
O<sub>3</sub>
content. The following order of basicity was observed: Co(0)/5 wt.%La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
< Co(0)/10 wt.%La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
«Co(O)/50 wt.%La<sub>2</sub>
O<sub>3</sub>
-SiO<sub>2</sub>
. The addition of La<sub>2</sub>
O<sub>3</sub>
to the Co(O)/SiO<sub>2</sub>
reference sample revealed a very positive effect on the catalytic stability of catalysts. La<sub>2</sub>
O<sub>3</sub>
prevented cobalt phase sintering by avoiding particle coalescence.</s0>
</fC01>
<fC02 i1="01" i2="X"><s0>001C01A03B</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Basicité</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Alkalinity</s0>
<s5>01</s5>
</fC03>
<fC03 i1="01" i2="X" l="SPA"><s0>Alcalinidad</s0>
<s5>01</s5>
</fC03>
<fC03 i1="02" i2="X" l="FRE"><s0>Lanthane oxyde</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="ENG"><s0>Lanthanum oxide</s0>
<s5>02</s5>
</fC03>
<fC03 i1="02" i2="X" l="SPA"><s0>Lantano óxido</s0>
<s5>02</s5>
</fC03>
<fC03 i1="03" i2="X" l="FRE"><s0>Silice</s0>
<s1>ACT</s1>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Silica</s0>
<s1>ACT</s1>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="03" i2="X" l="SPA"><s0>Sílice</s0>
<s1>ACT</s1>
<s2>NK</s2>
<s2>FX</s2>
<s5>03</s5>
</fC03>
<fC03 i1="04" i2="X" l="FRE"><s0>Carbone dioxyde</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="ENG"><s0>Carbon dioxide</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>04</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Carbono dióxido</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>04</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Méthane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Methane</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>05</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Metano</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>05</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Reformage</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Reforming</s0>
<s5>06</s5>
</fC03>
<fC03 i1="06" i2="X" l="SPA"><s0>Reformación</s0>
<s5>06</s5>
</fC03>
<fC03 i1="07" i2="X" l="FRE"><s0>Catalyseur</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="ENG"><s0>Catalyst</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Catalizador</s0>
<s5>07</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Additif</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Additive</s0>
<s5>08</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Aditivo</s0>
<s5>08</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Cobalt Oxyde</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Cobalt Oxides</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>09</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Cobalto Óxido</s0>
<s1>ACT</s1>
<s2>NC</s2>
<s2>NA</s2>
<s5>09</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Activité catalytique</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Catalyst activity</s0>
<s5>10</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Actividad catalítica</s0>
<s5>10</s5>
</fC03>
<fN21><s1>016</s1>
</fN21>
</pA>
<pR><fA30 i1="01" i2="1" l="ENG"><s1>International Symposium on Calorimetry and Thermal Effects in Catalysis</s1>
<s2>3</s2>
<s3>Lyon FRA</s3>
<s4>2004-07-06</s4>
</fA30>
</pR>
</standard>
</inist>
</record>
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