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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Format: | EJournal Article |
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Department of Chemical Engineering - Diponegoro University,
2016-08-20.
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LEADER | 02419 am a22002893u 4500 | ||
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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 |