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Catalytic methane pyrolysis for simultaneous production of hydrogen and graphitic carbon using a ceramic sparger in a molten NiSn alloy
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Publication Year
2023-04-01
Publisher
Elsevier Ltd
Citation
Carbon, Vol.207, pp.1-12
Keyword
Catalytic methane pyrolysisCeramic spargerGraphitic carbonHydrogen productionMolten alloy catalystNiSn alloy
Mesh Keyword
Alloy catalystCatalytic methane pyrolyseCeramic spargeCH 4Graphitic carbonsMethane pyrolysisMolten alloyMolten alloy catalystNi-sn alloysProduction of hydrogen
All Science Classification Codes (ASJC)
Chemistry (all)Materials Science (all)
Abstract
Catalytic methane pyrolysis (CMP) for simultaneous hydrogen and carbon production has been achieved in molten NiSn liquid alloys, with the additional benefit of spontaneous separation of solid carbon from the liquid catalyst. Here, the use of ceramic spargers for the injection of CH4 bubbles into the molten liquid has shown to be advantageous not only in enhancing the CH4 conversion above 90%, but also in producing graphitic carbon. When a quartz tube was used to feed CH4 bubbles into the molten alloy, the conversation was limited to about 15–25% and the quality of the graphitic carbon product was more defective and disordered. Regardless of the use of the spargers, carbon precipitates preferentially accumulate at the top of the molten alloy, and steady-state conversion over 24 h with high selectivity towards H2 was achieved under a constant flow rate of pure CH4 without any pressure increase. The synergistic effect of the ceramic sparger on molten NiSn may be the result of a controlled bubble size of CH4 and a catalytic role of zirconia surfaces in contact with the molten alloy. Our results imply that there is a great opportunity to improve CMP in molten alloy catalysts further toward a scalable production of H2 and graphitic carbon with a nearly complete conversion of CH4.
ISSN
0008-6223
Language
eng
URI
https://dspace.ajou.ac.kr/dev/handle/2018.oak/33289
DOI
https://doi.org/10.1016/j.carbon.2023.02.053
Fulltext

Type
Article
Funding
This research was supported by C1 Gas Refinery Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science and ICT ( NRF-2021M3D3A1A01079484 , NRF-2022M3J5A1085252 ).
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SEO, HYUNGTAK서형탁
Department of Materials Science Engineering
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