Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts

Hydrogen production from the direct thermo-catalytic decomposition of methane is a promising alter-native for clean fuel production. However, thermal decomposition of methane can hardly be of any practical and empirical interest in the industry unless highly efficient and effective catalysts, in ter...

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Main Authors: Lock, Irene S. M., Lock, Serene S. M., Vo, Dai-Viet N., Bawadi, Abdullah
Format: Article
Language:English
Published: Department of Chemical Engineering, Diponegoro University 2016
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Online Access:http://umpir.ump.edu.my/id/eprint/13554/1/550-1002-3-PB_Viet%20Vo.pdf
http://umpir.ump.edu.my/id/eprint/13554/
http://dx.doi.org/10.9767/bcrec.11.2.550.191-199
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spelling my.ump.umpir.135542018-11-30T02:08:37Z http://umpir.ump.edu.my/id/eprint/13554/ Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts Lock, Irene S. M. Lock, Serene S. M. Vo, Dai-Viet N. Bawadi, Abdullah TP Chemical technology Hydrogen production from the direct thermo-catalytic decomposition of methane is a promising alter-native for clean fuel production. However, thermal decomposition of methane can hardly be of any practical and empirical interest in the industry unless highly efficient and effective catalysts, in terms of both catalytic activity and operational lifetime have been developed. In this study, the effect of palladium (Pd) as a promoter onto Ni supported on alumina catalyst has been investigated by using co-precipitation technique. The introduction of Pd promotes better catalytic activity, operational lifetime and thermal stability of the catalyst. As expected, highest methane conversion was achieved at reaction temperature of 800 °C while the bimetallic catalyst (1 wt.% Ni -1 wt.% Pd/Al2O3) gave the highest methane conversion of 70% over 15 min of time-on-stream (TOS). Interestingly, the introduction of Pd as promoter onto Ni-based catalyst also has a positive effect on the operational lifetime and thermal stability of the catalyst as the methane conversion has improved significantly over 240 min of TOS. Department of Chemical Engineering, Diponegoro University 2016 Article PeerReviewed application/pdf en cc_by_sa http://umpir.ump.edu.my/id/eprint/13554/1/550-1002-3-PB_Viet%20Vo.pdf Lock, Irene S. M. and Lock, Serene S. M. and Vo, Dai-Viet N. and Bawadi, Abdullah (2016) Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts. Bulletin of Chemical Reaction Engineering & Catalysis, 11 (2). pp. 191-199. ISSN 1978-2993 http://dx.doi.org/10.9767/bcrec.11.2.550.191-199 DOI: 10.9767/bcrec.11.2.550.191-199
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Lock, Irene S. M.
Lock, Serene S. M.
Vo, Dai-Viet N.
Bawadi, Abdullah
Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts
description Hydrogen production from the direct thermo-catalytic decomposition of methane is a promising alter-native for clean fuel production. However, thermal decomposition of methane can hardly be of any practical and empirical interest in the industry unless highly efficient and effective catalysts, in terms of both catalytic activity and operational lifetime have been developed. In this study, the effect of palladium (Pd) as a promoter onto Ni supported on alumina catalyst has been investigated by using co-precipitation technique. The introduction of Pd promotes better catalytic activity, operational lifetime and thermal stability of the catalyst. As expected, highest methane conversion was achieved at reaction temperature of 800 °C while the bimetallic catalyst (1 wt.% Ni -1 wt.% Pd/Al2O3) gave the highest methane conversion of 70% over 15 min of time-on-stream (TOS). Interestingly, the introduction of Pd as promoter onto Ni-based catalyst also has a positive effect on the operational lifetime and thermal stability of the catalyst as the methane conversion has improved significantly over 240 min of TOS.
format Article
author Lock, Irene S. M.
Lock, Serene S. M.
Vo, Dai-Viet N.
Bawadi, Abdullah
author_facet Lock, Irene S. M.
Lock, Serene S. M.
Vo, Dai-Viet N.
Bawadi, Abdullah
author_sort Lock, Irene S. M.
title Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts
title_short Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts
title_full Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts
title_fullStr Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts
title_full_unstemmed Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts
title_sort thermo-catalytic methane decomposition for hydrogen production: effect of palladium promoter on ni-based catalysts
publisher Department of Chemical Engineering, Diponegoro University
publishDate 2016
url http://umpir.ump.edu.my/id/eprint/13554/1/550-1002-3-PB_Viet%20Vo.pdf
http://umpir.ump.edu.my/id/eprint/13554/
http://dx.doi.org/10.9767/bcrec.11.2.550.191-199
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