Hydrogenolysis of n-Butane over Ru/AlO Catalysts

Preliminary studies were undertaken of the preparation parameters of DIM (double impregnation method) influencing metal loading, ruthenium catalyst dispersion and n-butane hydrogenolysis. Ruthenium red was used as the metal precursor of Ru/Al 2 O 3 catalysts. The infrared spectra of ruthenium red an...

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Main Authors: Janusz Ryczkowski, Marcin Kuśmierz, Dobiesław Nazimek, Sylwia Pasieczna
Format: Article
Language:English
Published: Hindawi - SAGE Publishing 2002-12-01
Series:Adsorption Science & Technology
Online Access:https://doi.org/10.1260/026361702321705276
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spelling doaj-f588a441432246f189e24b99eb1701882021-04-02T13:32:46ZengHindawi - SAGE PublishingAdsorption Science & Technology0263-61742048-40382002-12-012010.1260/026361702321705276Hydrogenolysis of n-Butane over Ru/AlO CatalystsJanusz RyczkowskiMarcin KuśmierzDobiesław NazimekSylwia PasiecznaPreliminary studies were undertaken of the preparation parameters of DIM (double impregnation method) influencing metal loading, ruthenium catalyst dispersion and n-butane hydrogenolysis. Ruthenium red was used as the metal precursor of Ru/Al 2 O 3 catalysts. The infrared spectra of ruthenium red and EDTA adsorbed on alumina indicated that interaction occurs between adsorbates and the support surface. An extension of the impregnation time by ruthenium red caused a slight shift of the asymmetric –COO − band that may be explained by interaction between ruthenium and adsorbed EDTA. The small change in the –COO − band position was due to the nature of the metal–EDTA bond formed. An increase in metal loading led to an increase in ruthenium dispersion. Measurements of the rate of hydrogenolysis of n-butane were carried out in a gradientless reactor. All kinetic experiments were conducted under conditions where the hydrogen/n-butane molar ratio was 9:1, and involved isothermal determination of the relationship between the n-butane reaction rate and the corresponding degree of conversion (iso-X). The absence of propane and the presence of isobutane (at lower temperature) among the products were discussed.https://doi.org/10.1260/026361702321705276
collection DOAJ
language English
format Article
sources DOAJ
author Janusz Ryczkowski
Marcin Kuśmierz
Dobiesław Nazimek
Sylwia Pasieczna
spellingShingle Janusz Ryczkowski
Marcin Kuśmierz
Dobiesław Nazimek
Sylwia Pasieczna
Hydrogenolysis of n-Butane over Ru/AlO Catalysts
Adsorption Science & Technology
author_facet Janusz Ryczkowski
Marcin Kuśmierz
Dobiesław Nazimek
Sylwia Pasieczna
author_sort Janusz Ryczkowski
title Hydrogenolysis of n-Butane over Ru/AlO Catalysts
title_short Hydrogenolysis of n-Butane over Ru/AlO Catalysts
title_full Hydrogenolysis of n-Butane over Ru/AlO Catalysts
title_fullStr Hydrogenolysis of n-Butane over Ru/AlO Catalysts
title_full_unstemmed Hydrogenolysis of n-Butane over Ru/AlO Catalysts
title_sort hydrogenolysis of n-butane over ru/alo catalysts
publisher Hindawi - SAGE Publishing
series Adsorption Science & Technology
issn 0263-6174
2048-4038
publishDate 2002-12-01
description Preliminary studies were undertaken of the preparation parameters of DIM (double impregnation method) influencing metal loading, ruthenium catalyst dispersion and n-butane hydrogenolysis. Ruthenium red was used as the metal precursor of Ru/Al 2 O 3 catalysts. The infrared spectra of ruthenium red and EDTA adsorbed on alumina indicated that interaction occurs between adsorbates and the support surface. An extension of the impregnation time by ruthenium red caused a slight shift of the asymmetric –COO − band that may be explained by interaction between ruthenium and adsorbed EDTA. The small change in the –COO − band position was due to the nature of the metal–EDTA bond formed. An increase in metal loading led to an increase in ruthenium dispersion. Measurements of the rate of hydrogenolysis of n-butane were carried out in a gradientless reactor. All kinetic experiments were conducted under conditions where the hydrogen/n-butane molar ratio was 9:1, and involved isothermal determination of the relationship between the n-butane reaction rate and the corresponding degree of conversion (iso-X). The absence of propane and the presence of isobutane (at lower temperature) among the products were discussed.
url https://doi.org/10.1260/026361702321705276
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AT marcinkusmierz hydrogenolysisofnbutaneoverrualocatalysts
AT dobiesławnazimek hydrogenolysisofnbutaneoverrualocatalysts
AT sylwiapasieczna hydrogenolysisofnbutaneoverrualocatalysts
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