Thermocatalytic decomposition of methane for hydrogen production using activated carbon catalyst: Regeneration and characterization studies

Abbas, Hazzim F. and Daud, Wan Mohd Ashri Wan (2009) Thermocatalytic decomposition of methane for hydrogen production using activated carbon catalyst: Regeneration and characterization studies. International Journal of Hydrogen Energy, 34 (19). pp. 8034-8045. ISSN 0360-3199, DOI https://doi.org/10.1016/j.ijhydene.2009.08.014.

Full text not available from this repository.
Official URL: https://doi.org/10.1016/j.ijhydene.2009.08.014

Abstract

A series of experiments was conducted to study the deactivation and regeneration of activated carbon catalyst used for methane thermocatalytic decomposition to produce hydrogen. The catalyst becomes deactivated due to carbon deposition and six decomposition cycles of methane at temperatures of 850 and 950 °C, and five cycles of regeneration by using CO2 at temperatures of 900, 950 and 1000 °C were carried out to evaluate the stability of the catalyst. The experiment was conducted by using a thermobalance by monitoring the mass gain during decomposition or the mass lost during the regeneration with time. The initial activity and the ultimate mass gain of the catalyst decreased after each regeneration cycle at both reaction temperatures of 850 and 950 °C, but the amount is smaller under the more severe regenerating conditions. For the reaction at 950 °C, comparison between the first and sixth reaction cycles shows that the initial activity decreased by 69, 51 and 42%, while the ultimate mass gain decreased by 62%, 36% and 16% when CO2 gasification carried out at 900, 950 and 1000 °C respectively. Temperature -programmed oxidation profiles for the deactivated catalyst at reaction temperature of 950 °C and after several cycles showed two peaks which are attributed to different carbon characteristics, while one peak was obtained when the experiment was carried out at 850 °C. In conclusion, conducting methane decomposition at 950 °C and regeneration at 1000 °C showed the lowest decrease in the mass gain with reaction cycles. © 2009 Professor T. Nejat Veziroglu.

Item Type: Article
Funders: Institute of postgraduate studies/University of Malaya
Uncontrolled Keywords: Regeneration; Catalytic methane decomposition; Hydrogen production; Activated carbon; Characterization
Subjects: T Technology > TP Chemical technology
Divisions: Faculty of Engineering
Depositing User: Ms. Juhaida Abd Rahim
Date Deposited: 16 Oct 2020 00:37
Last Modified: 16 Oct 2020 00:37
URI: http://eprints.um.edu.my/id/eprint/25565

Actions (login required)

View Item View Item