Data di Pubblicazione:
2016
Abstract:
This paper covers the research activities performed at the CNR Institute for Advanced Energy Technologies "Nicola Giordano", aimed at developing and testing a biogas steam reforming reactor. A mathematical model has been developed in order to describe, the performance of the above-cited steam reforming reactor (packed bed). To study the effects on reaction performance, a parametric analysis was performed varying operating conditions such as inlet temperature and reagent molar ratio. The model was validated by comparing the calculated data with the experimental data obtained with a proprietary Ni/ CeO2 based catalyst in packet bed micro-scale reactor at different T ¼ 700e900 C, S/C ¼ 1e5 and GHSV ¼ 30,000 h1, showing a good agreement between the experimental and theoretical results.
Tipologia CRIS:
01.01 Articolo in rivista
Keywords:
Biogas; Steam reforming; Hydrogen Production; Fixed bed reactor; Heterogeneus catalysis
Elenco autori:
Italiano, Cristina; Vita, ANTONIO SALVATORE; Cipiti', Francesco; Giacoppo, Giosue'; Barbera, Orazio; Briguglio, Nicola
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