NickelMaghrebV1, PascalFrancis, Corpus, bibRecord, 000298

Microcalorimetric studies and methane reforming by CO2 on Ni-based zeolite catalysts

Identifieur interne : 000298 ( PascalFrancis/Corpus ); précédent : 000297; suivant : 000299

Microcalorimetric studies and methane reforming by CO2 on Ni-based zeolite catalysts

Auteurs : D. Halliche ; O. Cherifi ; A. Auroux

Source :

Thermochimica acta [ 0040-6031 ] ; 2005.

RBID : Pascal:06-0044720

Descripteurs français

Pascal (Inist)
- Microcalorimétrie, Méthane, Reformage, Carbone dioxyde, Zéolite, Catalyseur, Tamis moléculaire, Catalyse hétérogène, Isotherme adsorption, Analyse thermique.

English descriptors

KwdEn :
- Adsorption isotherm, Carbon dioxide, Catalyst, Heterogeneous catalysis, Methane, Microcalorimetry, Molecular sieve, Reforming, Thermal analysis, Zeolite.

Abstract

A series of catalysts containing nickel, based on HZSM-5 and USY zeolites, have been prepared by ionic exchange; a Ni/γ-Al₂O₃ catalyst has been prepared by impregnation, for comparison. Ammonia and CO adsorption microcalorimetry and temperature programmed reduction experiments have shown that NiZSM-5 is the most acidic and the most reducible catalyst. The study of the reaction of methane reforming by carbon dioxide in presence of these catalysts has shown that the catalytic performance depends simultaneously on the acidity, reducibility, and structure of the zeolite. Globally, it appears that the catalytic properties of NiUSY are superior to those of NiZSM-5 and Ni/γ-Al₂O₃.

Notice en format standard (ISO 2709)

Pour connaître la documentation sur le format Inist Standard.

A01	`01`	`1`		`@0 0040-6031`
A02	`01`			`@0 THACAS`
A03		`1`		`@0 Thermochim. acta`
A05				`@2 434`
A06				`@2 1-2`
A08	`01`	`1`	`ENG`	`@1 Microcalorimetric studies and methane reforming by CO₂ on Ni-based zeolite catalysts`
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 HALLICHE (D.)`
A11	`02`	`1`		`@1 CHERIFI (O.)`
A11	`03`	`1`		`@1 AUROUX (A.)`
A12	`01`	`1`		`@1 AUROUX (Aline) @9 ed.`
A14	`01`			`@1 Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB, BP32 @2 El-Alia, Alger @3 DZA @Z 1 aut. @Z 2 aut.`
A14	`02`			`@1 Institut de Recherches sur la Catalyse, CNRS, 2 av. Albert Einstein @2 69626 Villeurbanne @3 FRA @Z 3 aut.`
A15	`01`			`@1 CNRS, Institut de Recherches sur la Catalyse, 2 avenue A. Einstein @2 69626 Villeurbanne @3 FRA @Z 1 aut.`
A20				`@1 125-131`
A21				`@1 2005`
A23	`01`			`@0 ENG`
A43	`01`			`@1 INIST @2 14753 @5 354000131483590200`
A44				`@0 0000 @1 © 2006 INIST-CNRS. All rights reserved.`
A45				`@0 46 ref.`
A47	`01`	`1`		`@0 06-0044720`
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 catalysts containing nickel, based on HZSM-5 and USY zeolites, have been prepared by ionic exchange; a Ni/γ-Al₂O₃ catalyst has been prepared by impregnation, for comparison. Ammonia and CO adsorption microcalorimetry and temperature programmed reduction experiments have shown that NiZSM-5 is the most acidic and the most reducible catalyst. The study of the reaction of methane reforming by carbon dioxide in presence of these catalysts has shown that the catalytic performance depends simultaneously on the acidity, reducibility, and structure of the zeolite. Globally, it appears that the catalytic properties of NiUSY are superior to those of NiZSM-5 and Ni/γ-Al₂O₃.
C02	`01`	`X`		`@0 001C01A03B`
C03	`01`	`X`	`FRE`	`@0 Microcalorimétrie @5 01`
C03	`01`	`X`	`ENG`	`@0 Microcalorimetry @5 01`
C03	`01`	`X`	`SPA`	`@0 Microcalorimetría @5 01`
C03	`02`	`X`	`FRE`	`@0 Méthane @2 NK @2 FX @5 02`
C03	`02`	`X`	`ENG`	`@0 Methane @2 NK @2 FX @5 02`
C03	`02`	`X`	`SPA`	`@0 Metano @2 NK @2 FX @5 02`
C03	`03`	`X`	`FRE`	`@0 Reformage @5 03`
C03	`03`	`X`	`ENG`	`@0 Reforming @5 03`
C03	`03`	`X`	`SPA`	`@0 Reformación @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 Zéolite @5 05`
C03	`05`	`X`	`ENG`	`@0 Zeolite @5 05`
C03	`05`	`X`	`SPA`	`@0 Zeolita @5 05`
C03	`06`	`X`	`FRE`	`@0 Catalyseur @5 06`
C03	`06`	`X`	`ENG`	`@0 Catalyst @5 06`
C03	`06`	`X`	`SPA`	`@0 Catalizador @5 06`
C03	`07`	`X`	`FRE`	`@0 Tamis moléculaire @5 07`
C03	`07`	`X`	`ENG`	`@0 Molecular sieve @5 07`
C03	`07`	`X`	`SPA`	`@0 Tamiz molecular @5 07`
C03	`08`	`X`	`FRE`	`@0 Catalyse hétérogène @5 08`
C03	`08`	`X`	`ENG`	`@0 Heterogeneous catalysis @5 08`
C03	`08`	`X`	`SPA`	`@0 Catálisis heterogénea @5 08`
C03	`09`	`X`	`FRE`	`@0 Isotherme adsorption @5 09`
C03	`09`	`X`	`ENG`	`@0 Adsorption isotherm @5 09`
C03	`09`	`X`	`SPA`	`@0 Isotermo adsorción @5 09`
C03	`10`	`X`	`FRE`	`@0 Analyse thermique @5 32`
C03	`10`	`X`	`ENG`	`@0 Thermal analysis @5 32`
C03	`10`	`X`	`SPA`	`@0 Análisis térmico @5 32`
N21				`@1 023`

A30	`01`	`1`	`ENG`	`@1 International Symposium on Calorimetry and Thermal Effects in Catalysis @2 3 @3 Lyon FRA @4 2004-07-06`

Format Inist (serveur)

NO :	PASCAL 06-0044720 INIST
ET :	Microcalorimetric studies and methane reforming by CO₂ on Ni-based zeolite catalysts
AU :	HALLICHE (D.); CHERIFI (O.); AUROUX (A.); AUROUX (Aline)
AF :	Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB, BP32/El-Alia, Alger/Algérie (1 aut., 2 aut.); Institut de Recherches sur la Catalyse, CNRS, 2 av. Albert Einstein/69626 Villeurbanne/France (3 aut.); CNRS, Institut de Recherches sur la Catalyse, 2 avenue A. Einstein/69626 Villeurbanne/France (1 aut.)
DT :	Publication en série; Congrès; Niveau analytique
SO :	Thermochimica acta; ISSN 0040-6031; Coden THACAS; Pays-Bas; Da. 2005; Vol. 434; No. 1-2; Pp. 125-131; Bibl. 46 ref.
LA :	Anglais
EA :	A series of catalysts containing nickel, based on HZSM-5 and USY zeolites, have been prepared by ionic exchange; a Ni/γ-Al₂O₃ catalyst has been prepared by impregnation, for comparison. Ammonia and CO adsorption microcalorimetry and temperature programmed reduction experiments have shown that NiZSM-5 is the most acidic and the most reducible catalyst. The study of the reaction of methane reforming by carbon dioxide in presence of these catalysts has shown that the catalytic performance depends simultaneously on the acidity, reducibility, and structure of the zeolite. Globally, it appears that the catalytic properties of NiUSY are superior to those of NiZSM-5 and Ni/γ-Al₂O₃.
CC :	001C01A03B
FD :	Microcalorimétrie; Méthane; Reformage; Carbone dioxyde; Zéolite; Catalyseur; Tamis moléculaire; Catalyse hétérogène; Isotherme adsorption; Analyse thermique
ED :	Microcalorimetry; Methane; Reforming; Carbon dioxide; Zeolite; Catalyst; Molecular sieve; Heterogeneous catalysis; Adsorption isotherm; Thermal analysis
SD :	Microcalorimetría; Metano; Reformación; Carbono dióxido; Zeolita; Catalizador; Tamiz molecular; Catálisis heterogénea; Isotermo adsorción; Análisis térmico
LO :	INIST-14753.354000131483590200
ID :	06-0044720

Links to Exploration step

Pascal:06-0044720

Le document en format XML

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<term>Thermal analysis</term>
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<term>Catalyseur</term>
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<front><div type="abstract" xml:lang="en">A series of catalysts containing nickel, based on HZSM-5 and USY zeolites, have been prepared by ionic exchange; a Ni/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalyst has been prepared by impregnation, for comparison. Ammonia and CO adsorption microcalorimetry and temperature programmed reduction experiments have shown that NiZSM-5 is the most acidic and the most reducible catalyst. The study of the reaction of methane reforming by carbon dioxide in presence of these catalysts has shown that the catalytic performance depends simultaneously on the acidity, reducibility, and structure of the zeolite. Globally, it appears that the catalytic properties of NiUSY are superior to those of NiZSM-5 and Ni/γ-Al<sub>2</sub>
O<sub>3</sub>
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<fA08 i1="01" i2="1" l="ENG"><s1>Microcalorimetric studies and methane reforming by CO<sub>2</sub>
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<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>
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<fA11 i1="01" i2="1"><s1>HALLICHE (D.)</s1>
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<fA12 i1="01" i2="1"><s1>AUROUX (Aline)</s1>
<s9>ed.</s9>
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<fA14 i1="01"><s1>Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB, BP32</s1>
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<sZ>1 aut.</sZ>
<sZ>2 aut.</sZ>
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<fA14 i1="02"><s1>Institut de Recherches sur la Catalyse, CNRS, 2 av. Albert Einstein</s1>
<s2>69626 Villeurbanne</s2>
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<sZ>3 aut.</sZ>
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<fA15 i1="01"><s1>CNRS, Institut de Recherches sur la Catalyse, 2 avenue A. Einstein</s1>
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<fC01 i1="01" l="ENG"><s0>A series of catalysts containing nickel, based on HZSM-5 and USY zeolites, have been prepared by ionic exchange; a Ni/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalyst has been prepared by impregnation, for comparison. Ammonia and CO adsorption microcalorimetry and temperature programmed reduction experiments have shown that NiZSM-5 is the most acidic and the most reducible catalyst. The study of the reaction of methane reforming by carbon dioxide in presence of these catalysts has shown that the catalytic performance depends simultaneously on the acidity, reducibility, and structure of the zeolite. Globally, it appears that the catalytic properties of NiUSY are superior to those of NiZSM-5 and Ni/γ-Al<sub>2</sub>
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<s2>NK</s2>
<s2>FX</s2>
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<s5>03</s5>
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<s5>03</s5>
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<fC03 i1="04" i2="X" l="FRE"><s0>Carbone dioxyde</s0>
<s2>NK</s2>
<s2>FX</s2>
<s5>04</s5>
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<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>
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<fC03 i1="05" i2="X" l="FRE"><s0>Zéolite</s0>
<s5>05</s5>
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<fC03 i1="05" i2="X" l="ENG"><s0>Zeolite</s0>
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<fC03 i1="05" i2="X" l="SPA"><s0>Zeolita</s0>
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<s5>06</s5>
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<s5>08</s5>
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<s5>09</s5>
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<s5>32</s5>
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<fN21><s1>023</s1>
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<pR><fA30 i1="01" i2="1" l="ENG"><s1>International Symposium on Calorimetry and Thermal Effects in Catalysis</s1>
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<s4>2004-07-06</s4>
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</standard>
<server><NO>PASCAL 06-0044720 INIST</NO>
<ET>Microcalorimetric studies and methane reforming by CO<sub>2</sub>
 on Ni-based zeolite catalysts</ET>
<AU>HALLICHE (D.); CHERIFI (O.); AUROUX (A.); AUROUX (Aline)</AU>
<AF>Laboratoire de Chimie du Gaz Naturel, Faculté de Chimie, USTHB, BP32/El-Alia, Alger/Algérie (1 aut., 2 aut.); Institut de Recherches sur la Catalyse, CNRS, 2 av. Albert Einstein/69626 Villeurbanne/France (3 aut.); CNRS, Institut de Recherches sur la Catalyse, 2 avenue A. Einstein/69626 Villeurbanne/France (1 aut.)</AF>
<DT>Publication en série; Congrès; Niveau analytique</DT>
<SO>Thermochimica acta; ISSN 0040-6031; Coden THACAS; Pays-Bas; Da. 2005; Vol. 434; No. 1-2; Pp. 125-131; Bibl. 46 ref.</SO>
<LA>Anglais</LA>
<EA>A series of catalysts containing nickel, based on HZSM-5 and USY zeolites, have been prepared by ionic exchange; a Ni/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalyst has been prepared by impregnation, for comparison. Ammonia and CO adsorption microcalorimetry and temperature programmed reduction experiments have shown that NiZSM-5 is the most acidic and the most reducible catalyst. The study of the reaction of methane reforming by carbon dioxide in presence of these catalysts has shown that the catalytic performance depends simultaneously on the acidity, reducibility, and structure of the zeolite. Globally, it appears that the catalytic properties of NiUSY are superior to those of NiZSM-5 and Ni/γ-Al<sub>2</sub>
O<sub>3</sub>
.</EA>
<CC>001C01A03B</CC>
<FD>Microcalorimétrie; Méthane; Reformage; Carbone dioxyde; Zéolite; Catalyseur; Tamis moléculaire; Catalyse hétérogène; Isotherme adsorption; Analyse thermique</FD>
<ED>Microcalorimetry; Methane; Reforming; Carbon dioxide; Zeolite; Catalyst; Molecular sieve; Heterogeneous catalysis; Adsorption isotherm; Thermal analysis</ED>
<SD>Microcalorimetría; Metano; Reformación; Carbono dióxido; Zeolita; Catalizador; Tamiz molecular; Catálisis heterogénea; Isotermo adsorción; Análisis térmico</SD>
<LO>INIST-14753.354000131483590200</LO>
<ID>06-0044720</ID>
</server>
</inist>
</record>

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Microcalorimetric studies and methane reforming by CO2 on Ni-based zeolite catalysts

Microcalorimetric studies and methane reforming by CO2 on Ni-based zeolite catalysts

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