ThuliumV1, Main, Exploration, bibRecord, 002A83

Reforming of Pd-lanthanide catalysts

Identifieur interne : 002A83 ( Main/Exploration ); précédent : 002A82; suivant : 002A84

Reforming of Pd-lanthanide catalysts

Auteurs : N. Mahalakshmi Sita [Inde]

Source :

Indian journal of chemical technology [ 0971-457X ] ; 1997.

RBID : Pascal:97-0441293

Descripteurs français

Pascal (Inist)
- Reformage catalytique, Hydrocarbure, Cyclohexane, Heptane, Cyclopentane(méthyl), Catalyse hétérogène, Catalyseur sur support, Catalyseur mixte, Alumine, Palladium, Dysprosium, Holmium, Thulium, Activité catalytique, Site actif, Cinétique, Etude expérimentale.
Wicri :
- topic : Hydrocarbure.

English descriptors

KwdEn :
- Active site, Alumina, Catalyst activity, Catalytic reforming, Cyclohexane, Dysprosium, Experimental study, Heptane, Heterogeneous catalysis, Holmium, Hydrocarbon, Kinetics, Mixed catalyst, Palladium, Supported catalyst, Thulium.

Abstract

The reforming reactions of cyclohexane, methyl cyclopentane and n-heptane on the Pd/γ-Al₂O₃ and Pd-Ln/γ-Al₂O₃ (Ln=Dy, Ho, Tm) catalysts have been investigated. The results demonstrate that Pd-Ln/γ-Al₂O₃ catalysts evince high activity and stability compared to Pd/γ-Al₂O₃ catalysts. Owing to the different lanthanide content in the catalysts, the aromatisation and isomerization yields are different in the reforming reactions of n-heptane and cyclopentane. It is interesting to investigate the optimum content of lanthanides which gives the maximum aromatisation and isomerization yield.

Affiliations:

Inde

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

to stream Pascal, to step Corpus: 001358
to stream Pascal, to step Curation: 001358
to stream Pascal, to step Checkpoint: 001307
to stream Main, to step Merge: 002C79
to stream Main, to step Curation: 002A83

Le document en format XML

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<term>Catalytic reforming</term>
<term>Cyclohexane</term>
<term>Dysprosium</term>
<term>Experimental study</term>
<term>Heptane</term>
<term>Heterogeneous catalysis</term>
<term>Holmium</term>
<term>Hydrocarbon</term>
<term>Kinetics</term>
<term>Mixed catalyst</term>
<term>Palladium</term>
<term>Supported catalyst</term>
<term>Thulium</term>
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<keywords scheme="Pascal" xml:lang="fr"><term>Reformage catalytique</term>
<term>Hydrocarbure</term>
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<term>Cyclopentane(méthyl)</term>
<term>Catalyse hétérogène</term>
<term>Catalyseur sur support</term>
<term>Catalyseur mixte</term>
<term>Alumine</term>
<term>Palladium</term>
<term>Dysprosium</term>
<term>Holmium</term>
<term>Thulium</term>
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<front><div type="abstract" xml:lang="en">The reforming reactions of cyclohexane, methyl cyclopentane and n-heptane on the Pd/γ-Al<sub>2</sub>
O<sub>3</sub>
 and Pd-Ln/γ-Al<sub>2</sub>
O<sub>3</sub>
 (Ln=Dy, Ho, Tm) catalysts have been investigated. The results demonstrate that Pd-Ln/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalysts evince high activity and stability compared to Pd/γ-Al<sub>2</sub>
O<sub>3</sub>
 catalysts. Owing to the different lanthanide content in the catalysts, the aromatisation and isomerization yields are different in the reforming reactions of n-heptane and cyclopentane. It is interesting to investigate the optimum content of lanthanides which gives the maximum aromatisation and isomerization yield.</div>
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Reforming of Pd-lanthanide catalysts

Reforming of Pd-lanthanide catalysts

Source :

Descripteurs français

English descriptors

Abstract

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

Le document en format XML

Pour manipuler ce document sous Unix (Dilib)

Pour mettre un lien sur cette page dans le réseau Wicri