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 alternative 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 term...

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Main Authors: Mei, Irene Lock Sow (Author), Lock, S.S.M (Author), Vo, Dai-Viet N. (Author), Abdullah, Bawadi (Author)
Format: EJournal Article
Published: Department of Chemical Engineering - Diponegoro University, 2016-08-20.
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001 BCREC_UNDIP_550_426
042 |a dc 
100 1 0 |a Mei, Irene Lock Sow  |e author 
100 1 0 |e contributor 
700 1 0 |a Lock, S.S.M.  |e author 
700 1 0 |a Vo, Dai-Viet N.  |e author 
700 1 0 |a Abdullah, Bawadi  |e author 
245 0 0 |a Thermo-Catalytic Methane Decomposition for Hydrogen Production: Effect of Palladium Promoter on Ni-based Catalysts 
260 |b Department of Chemical Engineering - Diponegoro University,   |c 2016-08-20. 
500 |a https://ejournal2.undip.ac.id/index.php/bcrec/article/view/550 
520 |a Hydrogen production from the direct thermo-catalytic decomposition of methane is a promising alternative 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 -1wt.% 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.  
540 |a Copyright (c) 2016 by Authors, Published by BCREC Group 
540 |a http://creativecommons.org/licenses/by-sa/4.0 
546 |a eng 
690 |a Methane cracking; TCD; Metal catalysts; Co-precipitation; Nobel metal 
655 7 |a info:eu-repo/semantics/article  |2 local 
655 7 |a info:eu-repo/semantics/publishedVersion  |2 local 
655 7 |2 local 
786 0 |n Bulletin of Chemical Reaction Engineering & Catalysis; 2016: BCREC Volume 11 Issue 2 Year 2016 (August 2016); 191-199 
786 0 |n 1978-2993 
787 0 |n https://ejournal2.undip.ac.id/index.php/bcrec/article/view/550/426 
856 4 1 |u https://ejournal2.undip.ac.id/index.php/bcrec/article/view/550/426  |z Get Fulltext